WO1992008674A1

WO1992008674A1 - A method for treating an organic substance

Info

Publication number: WO1992008674A1
Application number: PCT/DK1991/000347
Authority: WO
Inventors: Niels Ole Vesterager
Original assignee: Niels Ole Vesterager
Priority date: 1990-11-20
Filing date: 1991-11-20
Publication date: 1992-05-29
Also published as: ATE176893T1; DK0558568T3; ES2131509T3; DK278890D0; EP0558568A1; NO931856D0; EP0558568B1; DE69130925T2; NO306018B1; NO931856L; DE69130925D1

Abstract

It is possible to chemically treat a biomass in the form of domestic animal manure, slurry, organically loaded effluent waste water and the like, which makes it possible to separate the fertilizing substances N, P and K and to obtain a water fraction which meets the requirements for discharge directly to a recipient. This is obtained by treating fresh biomass mechanically and/or chemically, e.g. by simple precipitation and enzymatic decomposition of the fibre content or by degasification of the manure. Phorphorus and nitrogen in the pre-treated biomass are precipitated by adding chemical reactive agents. The reactive agents are caused to react with the nitrogen compounds and the phosphorus compounds present to form new compounds which can be precipitated. Any urea content is precipitated together with nitrogen and phosphorus. Potassium is also precipitated together with nitrogen and phosphorus before separation of the biomass into the liquid fraction and the fertilizer fraction. The chemical reactive agents comprise metal ions and organic and inorganic acids.

Description

A METHOD FOR TREATING AN ORGANIC SUBSTANCE

Background of the Invention.

The present invention relates to a method of treating a biomass in the form of domestic animal manure, slurry, organically loaded effluent waste water and the like, or mixtures thereof, and comprising a chemical treatment of the biomass.

Various methods are known in which a biomass is chemically treated in connection with the separation of the biomass. The chemical treatments are ordinarily used in connection with an adjustment of the pH-value of the liquid manure, e.g. in connection with biogas manufacture.

In the treatment of a biomass in the form of domestic animal manure, biologically loaded effluent waste water and the like, it has up to now been difficult to separate the biomass into components which may be utilized or which may directly be disposed of.

In connection with domestic animal manure, an insufficient separation has created the need for very large storage capacities. Furthermore, transport with the spreading of the very large quantities, which mainly are constituted by water, create certain problems, as the spreading is only allowed to be effected at certain times of the year. Several attempts have been made to separate the water and the nutrient salts in order to concentrate the nutrient salts into a small volume so as to make it possible to reduce the costs for storage and spreading. At the same time, the aim has been to sufficiently purify the water to allow it to be discharged directly to a recipient in order thereby to avoid the high disposal charges to the purification plant. Up to now, it has been difficult to sufficiently remove nitrogen, phosphorus and potassium from the water to allow the latter to be discharged directly to a recipient. In the treatment of domestic animal manure, it is also necessary to remove urea before allowing discharge of a water fraction. It is the object of the invention to remedy the above mentioned problems, not exclusively in connection with domestic animal manure but generally in connection with a biomass, by providing a method which makes it possible to separate the biomass into a small fraction which may be utilized as a fertilizer and a large fraction which may direct ly be discharged to a recipient. According to the invention this is obtained with a method which is characterized in pre-treating a fresh biomass mechnically and/or chemically, measuring NH₄ ⁺, and K⁺,

precipitating the nitrogen and phosphorus content of the pretreated biomass by adding in a stoichiometric ratio of 1:1 chemical reactive agents which are caused to react with the nitrogen compounds and the phosphorus compounds present in the biomass, precipitating any urea content together with the nitrogen, phosphorus and optional potassium content of the biomass, and subsequently separating the biomass into a liquid fraction and a fertilizer fraction.

Description of the Drawing.

The invention will now be explained in further detail with reference to the accompanying drawings wherein

Fig. 1 illustrates a flow chart for a method according to the invention, and

Fig. 2 illustrates a flow chart for an alternative method according to the invention.

Tank 1 is intended to receive the fresh biomass. In case of domestic animal manure, the tank 1 receives the liquid manure in a quantity corresponding to one day's production as it is desired to treat the liquid manure as fast as possible in order to limit the decomposition of urease to urea which may result in ammonification.

In tank 2 the fiber fraction is separated by adding a flocculation agent 14. The total fibre fraction 5 is discharged and transferred to tank 9 in which chemicals 13 are added to adjust the pH-value. Subsequently bacteria and enzymes are added to decompose the fibres and hence to liberate/extract nitrogen, phosphorus and potassium bound in the non-transformed fibre material. Thus, in tank 9 solid material is decomposed, e.g. lignocellulose, which facilitates a subsequent removal of N, P and K. N, P and K do not exist in the form of ions but are bound in the lignocellulose due to an incomplete biodegradation.

The pretreated fibre fraction is transferred from tank 9 to tank 3 in which it is mixed with the liquid fraction from tank 2 (from which the fibre fraction was previously separated). By adding metal ions and adjusting the pH-value, the urea complex, ammonium and phosphate are caused to precipitate in the acid to slightly alkaline solution. The selection of the added chemicals 11 depends on how the soil and plants will react on the precipitated fertilizer type.

In tank 3, two types of precipitation may be effected. Thus, an urea complex may be produced in which only urea is precipitated and (depending on the pH-value) ammonium ions may furthermore be precipitated from ammonia. Furthermore, phosphorus is precipitated. The nitrogen and phosphorus fractions as well as the urea complex are filtered off in a filter 4, and the liquid phase is transferred from tank 3 to tank 6 and the pH-value is adjusted so as to be approximately between 7.0 and 7.5. By adding metal ions and sulphate and phosphorus ions, (potassium ions) (inserted during translation, translator's remark) are precipitated as a double salt which is filtered off in a filter 7. The substances from the filters 4 and 7 may be mixed to form an organic fertilizer containing N, P and K. The liquid fraction is then transferred to a tank 8 and will consist of water which may be discharged directly into the external environment without violating public limit values for nitrogen and phosphorus content. The water will also be purified of potassium.

Thus, by means of the above method it is possible to obtain a water fraction which can be discharged directly and a fertilizer fraction which can be used as a dried fertilizer or as a dissolved fertilizer containing N, P and K. Thus, the costs of handling domestic animal manure are reduced. The environmental strain is reduced as N, P and K to a higher degree are recycled in the farming. In tests with the described proces it has proved possible to obtain 15-50 kg organic fertilizer from one m³ domestic animal manure, depending on the precipitation chemicals used. In the water fraction, residual concentrations of N and P as low as N_total = 1.5 ppm and P_total = 3.3 ppm are obtained, which allows a direct discharge to a recipient.

It is noted that the method according to the present invention may comprise another pre-treatment stage than the one shown in the process chart, as the pre-treatment prior to the transfer to tank 3 e.g. may consist of degasification or biogas formation so that the supply to tank 3 comprises degasified domestic animal manure. In the latter case, urea complex will not be precipitated in tank 3, as the urea content of the manure i s decomposed during the biogas formation. It will also be possible to carry out the method according to the invention without the chemical reaction in tank 6 in which the potassium fraction is precipitated. As potassium is not a critical factor for the discharge of effluent waste water, the liquid phase from tank 3 can be discharged directly to the recipient without removal of potassium. However, finansial consideration will decide whether the potassium fraction is removed from the effluent waste water before the latter is led out into the external environment.

In the following various test results and examples of the chemicals used in the various proces stages are given.

Tests have been made with domestic animal manure comprising urea, ammonium, phosphorus and potassium. In the tests, the effect of oxalic acid, COOH₂, nitric acid, HNO₃ and optionally phosphorus acid in connection with metal ions were investigated in depth with a view to precipitating compositions containing crytalline urea. Furthermore, magnesium sulfate, MgSO₄, 7 H₂O and manganese sulfate, MnSO₄, 4 H₂O are used to precipitate the crystalline metal complexes simultaneosuly for

NH₄ ⁺ and PO^-3 ₄.

Substances are formed which are sparingly soluble in an acid solution and these substances can thus be separated by means of the filter 4 (if a chemical reaction is also carried out to separate potassium, the separation will be carried out in the filter 7). The substances formed are non-hygroscopic, which means that they are free-flowing.

An analysis of the fibre fraction prior to the bio/enzymatic reaction shows the following: NH₃ P₂O₅ K₂O kg/m³ kg/m³ kg/m³

Untreated

biomass 4.25 1.55 5.83

Fibre fraction (5) 1.96 0.58 1.76

Biodegraded

material (tank 9) 1.53 0.42 1.28

Non-transferred

material 0.43 0.16 0.48

Thi s may also be illustrated in the following diagram

Total nitrogen converted into NH⁺ ₄

Analysi s of unAnalysis of Analysis of the treated sl urry the influx outflow from tank 9 from animal from tank 2 and 5 to tank 3 after husbandry to tank 9 prior bioreaction

to bioreaction

By changing the type of microorganisms, and the physical and chemical parameters in tank 8 it is possible to obtain very different yields for the decomposition of the lignocellulose based on the liberated quantities of N, P and K. As previously mentioned, N,P and K do not exist in the form of ions but are bound in the lignocellulose due to an incomplete biodegradation. It will be seen that the quantity of non-transferred materials is of almost the same size in tank 9 as in the discharge water from tank 8. A fibre fraction taken at step 5 shows a content of N < 0.1 kg/10001, P = 0 kg/10001, K < 0.25 kg/1000 1. An analysis of the mixture introduced into tank 3 from tanks 2 and 9 and the liquid fraction discharged from tank 3 shows the following results:

NH₃ P₂O₅ K₂O

kg/m³ kg/m³ kg/m³

Untreated liquid

manure for tank 3 4.25 1.55 5.83

Biodecomposition

in tank 9 1.53 0.42 1.28 Liquid fraction

from tank 2 2.29 0.97 4.07

Non-transferred

material in tank 9 0.43 0.16 0.48

After precipitation

in tank 3 0.46 0.17 5.83

This may also be expressed in a diagram

Analysis of unAnalysis of Analysis of the treated slurry the influx outflow from tank 3 from animal from tank 2 to tank 6 after husbandry and 9 to tank 3 bioreaction After the precipitation in tank 3, the liquid phase is optionally transferred to tank 6 in which an adjustment of pH is effected to precipitate the potassium content of the liquid. An analysis of the influx and the outflow from tank 6 shows the following:

NH₃ P₂O₅ K₂O kg/m³ kg/m³ kg/m³

Slurry from

animal husbandry 4.25 1.55 5.83

Influx to tank 6 0.46 0.17 5.83

Outflow from tank 8 0.46 0.17 0.48 Thi s may al so be expressed in a diagram.

Analysi s of unAnalysis of Analysis of the treated slurry the influx outflow from tank 6 from animal from tank 3 to tank 8 after husbandry to tank 6 precipitation

prior to

precipitation

The water flowing into tank 8 corresponds to the water discharged into the external environment. As a result of the method, N, P and K are reduced by approximately 90% compared to the liquid manure charged into the process.

Thus, the practical tests conducted have produced residual concentrations of nitrogen and phosphorus which are below the normally accepted limits for contents of effluent waste water discharged to a recipient. Thus, the water fraction in tank 8 can be led directly out into the external environment, and the N, P and K fractions can be collected in a tank 10 and used as a fertilizer. Specific examples of the chemicals used have been mentioned above, and the basic chemical reaction is based on the formation of sparingly soluble substances which can be caught in a filter. The basic chemical reactions forming part of the method according to the invention are based on a division of the nitrogen of the manure into four main categories:

1. Organically bound high molecular N,

2. Urea, CO(NH₂)₂,

3. Ammonium in ionic form NH₄ ⁺,

4. Ammonium NH, dissolved in water.

By adjusting pH it is possible to convert ammonia into the ionic form NH₄ ⁺. Two categories, urea and ammonium, can then be subjected to precipitation. Urea can be brought on ammonium form either enzymatically or over time, e.g. in a biogas proces.

The phosphorus in the slurry is divided into two main categories: 1. Fibre bound P,

2. Monohydrogenphosphate, as a residual product from metabolic

processes

Category 1 is small, and phosphorus will constitute a total of approximately 1/4 of the nitrogen content. This is a challenge to simultaneous precipitation.

The following gives examples of tests carried out with chemicals which are added as reactive agents.

1. Oxalic acid

Hypothesis: 2(NH₂)₂CO + (COOH)₂ Precipitation test according to the hypothesis:

Medium: urea corresponding to 5g N_total/l dissolved in deionized water. Reactive agent: oxalic acid dissolved in soft water to pH 2.

A residual product of N_total in a number of from 852, 697, and 707 ppm, respectively, was obtained. Each of these tests states an average of 5-15 individual tests and was carried out at pH-values of from 5.9, 2.77 and 3.45, respectively. The residual concentrations after precipitation of oxalic acid were not satisfactory, even though the molecular size of the urea complex indicates an advantageous flocculating ability which will be of significance when using slurry as a medium.

Nitric acid

Hypothesis: CO(NH₂)₂ + HNO₃ Precipitation tets according to the hypothesis.

Medium: urea corresponding to 5g N_total/l dissolved in deionized water. Reactive agent: nitric acid 70%..

In these tests, a residual product of N_total of 736 and 604 ppm, respectively, was obtained. These results are an average of 10 individual tests carried out at pH-values of from 5.90 and 2.77, respectively.

Magnesium sulfate

Hypothesis:

CO(NH₂)₂ → CO₂ + 2NH₃ NH₃ + H₃PO₄ →

→

Precipitation test according to the hypothesis.

Medium: ammonium corresponding to 5g N_total/l (5000 ppm) and cor

responding to 0.45 g P_total/l (450 ppm) dissolved in deionized water. Concentrations and proportions of N and P correspond to manure.

Reactive agents: Magnesium sulfate 0.1 mol/l

Trisodiumphosphate 0.1 mol/l

Sodiumcarbonate 0.1 mol/l

Phosphoric acid, concentrated.

These tests gave the following residual products.

Residual Residual Residual product product product

Test No. pH₁ PH₂ Mg⁺² ppm N_total ppm P_total ppm

1201 6.72 10.01 492 284 627

1202 6.80 10.19 138 80 177

1203 6.65 10.38 283 163 361

1204 6.84 10.56 419 242 536

The above main group of tests states an average of 5-20 individual tests at the pH 2 stated.

Manganese sulfate

Hypothesis:

CO(NH ₂)₂ → CO₂ + 2NH₃

NH₃ + H₃PO₄ →

→

→ NH₄MnPO_4.xH₂O

Precipitation test according to the hypothesis. Medium: ammonium corresponding to 5g N_total/1 (5000 ppm) and cor

Reactive agents: Manganese sulfate 0.1 mol/l

Trisodiumphosphate 0.1 mol/l

Sodiumcarbonate 0.1 mol/l

Phosphoric acid, concentrated.

These tests gave the following results.

Residual Residual Residual product product product

Test No. pH1 pH2 Mn⁺² ppm N_total ppm P_total ppm

2600 2.67 8.23 6 1.5 3.3

2601 2.97 10.77 1480 378.0 836

2602 2.77 7.45 27 12.5 27

2603 2.80 9.66 451 115.0 254

The above main groups of tests state an average of 5-20 individual tests at the pH 2 stated.

The tests conducted on precipitation of urea complexes have shown that the processes are feasible, even though the experimental yields have been lower than immediately would be expected with the pH range tested. An efficient precipitation can only take place under extreme acid conditions. The results show that the optimum of the process has not been reached even in chemically pure solutions. Extrapolation of the results indicates a more advantageous precipitation of the urea complex. Tests on simultaneous precipitation of phosphorus and ammonium with metals show high experimental yields. It has been found that the optimum process conditions have to be reached within a very narrow interval. Tests with a pH-value of about 8 have shown a remarkably efficient ammonium removal for manganese. Furthemore, manganese is preferred to magnesium due to the efficiency and a lower pH-value.

Examples of chemicals (11) for reactions in tank 3. n

Examples of chemicals (12) for reactions in tank 6.

Examples of chemicals (12) for reactions in tank 6 (cont.).

Fig. 2 illustrates a plant substantially like the one shown in Fig. 1, but in which a heat exchanger is inserted at the treatment stage treating the liquid fraction. This is associated with problems as there is a risk that a precipitate may be formed and the heat exchanger consequently may be blocked. This problem is solved by the present embodiment as two chemical process steps are carried out, one process step before and one process step after the heat exchanger, the first step i.a. ensuring that no precipitate is formed in the heat exchanger. Fresh manure is added to tank 1 and subsequently the fresh manure is transferred to a fibre separation step 2 in which the fibres present in the manure are separated from the fresh manure. The separated fibre amount 5 is passed to a composting plant 9 of a known type. However, the separation of fibres may optionally be omitted. The liquid fraction of the manure is passed to a pre-mixer 15 after the concentration of the following ions has been measured at point 16: ammonium ions, phosphate ions, carbonate ions and potassium ions. Depending on primarily the concentration of ammonium and carbonate, acid and (alkaline ions) (inserted during translation, translator's remark), preferably phosphate ions, H⁺ and X^n-, respectively, are added. The added acid ions, H⁺, are preferably derived from phosphorus acid, whereas the added base ions, X^n-, may be a phosphate-containing anion. This results in that the carbonate ion present in the liquid fraction is bound to the base ion and water and forms CO₂ which is liberated in the form of gas. In order to avoid precipitation in the heat exchanger 17, it is necessary to keep the acidity sufficiently low, which means a pH-value of from 5 or less, preferably 3.5. The liquid fraction is then passed through the heat exchanger 17 in which the temperature of the fraction is adjusted to between 40 and 50ºC, preferably 45ºC. After the liquid fraction has passed through the heat exchanger 17, it is passed to a after-mixer 18, in which adjustment of the acidity is repeated, but at this stage the purpose of the adjustment is to form fertilizing substances which can be precipitated. Preferably, the liquid fraction supplied to the after-mixer 18 has at the inlet 19 an acidity corresponding to pH = 3.5 as mentioned above. In the aftermixer various metal ions, M²⁺ _a and M²⁺ _b, and alkaline ions, B^m-, are added. The metal ions are preferably Mn-ions and Mg-ions, whereas the alkaline ions preferably are

-ions. However, other ions may also be used, but the addition of the above mentioned ions will result in the highest fertilizer value of the precipitates formed. The amount of the added ions is adjusted so that the pH-value is increased to between 7 and 9, preferably 8.2 and so that the substances which consequently may be precipitated are substances which can be used for fertilization or which are not sparingly soluble or in any other way damaging to the environment. In the addition of acid, metal and alkaline ions in the first and second proces step, respectively, the addition is exclusively effected in a stoichiometric ratio of 1:1. The following test descriptions with accompanying tables and graphic depictions illustrate that the ammonium content, either in the form of NH₄MnPO₄ or NH₄MgPO₄, has its lowest value at a temperature of about 45°C and at pH = 8.2. Moreover, it appears from the graphic depictions that in case zinc is used as a metal ion, pH must be in the range of between 8.5 and 9.1 in order have a minimum amount of ammonium ions. After the liquid fraction is made alkaline in the after-mixer 18 with a pH of about 8.2 measured at point 20, optionally by recirculating the fraction in the mixer, it is passed to a separator 21. In the separator, the temperature is reduced to between 10 and 12ºC and a separation of fertilizing substances is thus effected and the substances are precipitated. The liquid fraction which remains after the separation is very pure and can be discharged directly as effluent waste water 22 or to another recipient 23. In the separator 21, a degasification of CO₂ is effected provided the alkaline ions supplied to the after-mixer 18 are

. The precipitated fertilizing substances 24 are dried in a centrifuge and the liquid extracted is passed to a recipient 23. The dried nutrients 26 are mixed in a solid-matter mixer 27 with the fibre fraction 5 which was separated in 2 and composted in 9. An air drying may optionally be effected after the mixing at point 28. The described method results in a organic fertilizer mass 29 which is enriched with the nutrients 24 which are separated from the fresh manure as part of the method according to the invention.

In the following tables of results optained with a plant of the above mentioned type are tabulated.

Medium: ammonium corresponding to 5g N_total/l (5000 ppm) and cor

responding to 0.45 g P_total/l (450 ppm) dissolved in deionized water. Concentrations and proportions of N and P correspond to the degasified manure which is being processed. Reactive agents: Manganese chloride 0.5 mol/l

Phosphoric acid concentrated

Natrium carbonate 0.5 mol/l.

Test conditions:

The concentration of ammunion ions are maintained constant so as to correspond to 0.27 mol/l, equivalent amounts of phosphoric acid and manganese chloride are added, the resultant solution is heated to the temperatures stated for the test, the solution is then made alkaline by adding natrium carbonate so that pH = 8.2, which means pH is constant. Measurements are performed, i.e. a small sample of the liquid fraction is initially taken to determine the NHt. Subsequently, the precipitate is filtered off at vacuum and by washing with ion-exchanged water. The precipitate is dried at 80ºC for 48 hours before the concentration of NH₄ ⁺ in the precipitate is determined by dissolving the latter in mineral acid. The precipitate has the following composition: NH₄MnPO₄,H₂O.

These tests gave the following results.

[NH⁺ ₄]

Temperature in NH₄MnPO₄,H₂O

ºC (ppm)

20 302

30 73

40 22

45 9

50 11

60 64

70 295

Medium: ammonium corresponding to 5g NH₄/1 (5000 ppm) and PO₄ corresponding to 0.45 g P_total/1 (450 ppm) dissolved in deionized water. Concentrations and proportions of N and P correspond to the degasified manure which is being processed.

Reactive agents: Manganese chloride 0.5 mol/l

Phosphoric acid concentrated

Natrium carbonate 0.5 mol/l.

Test conditions: The concentration of ammunion ions are maintained constant so as to correspond to 0.27 mol/l, equivalent amounts of phosphoric acid and manganese chloride are added, the pH-value is measured (point 19) = pH,. The solution is then made alkaline with natrium carbonate. After addition of a varying amount of natrium carbonate, the pH-value is measured (point 20) = pH₂. The test is conducted by initially taking out a small sample of the liquid fraction to determine NH₄ and subsequently by separating the precipitate by filtration at vacuum and by washing with ion-exchanged water. The precipitate is dried at 80°C for 48 hours before determining the NH₄ content in NH₄MnPO₄,H₂O. These tests gave the following results.

Residual Residual product product

[NH⁺ ₄] ppm [NH⁺ ₄] ppm

Test No. pH₁ pH₂ in solution NH₄MnPO₄,H₂O

3609 1.54 4.05 2360 2571

3610 1.54 5.08 1204 3742

3611 1.54 5.88 592 4402

3612 1.54 6.91 152 4813

3613 1.54 7.45 13 4964

3614 1.54 8.02 7 4963

3615 1.54 8.24 2 4982

3616 1.54 8.92 98 4874

3617 1.54 9.08 334 4619

Claims

C L A I M S

1. A method of treating a biomass in the form of domestic animal manure, slurry, organically loaded effluent waste water and the like, or mixtures thereof, and comprising a chemical treatment of the biomass, c h a r a c t e r i z e d in pre-treating a fresh biomass mechnically and/or chemically, measuring NH⁺ ₄, and K⁺, precipitating the

nitrogen and phosphorus content of the pretreated biomass by adding in a stoichiometric ratio of 1:1 chemical reactive agents which are caused to react with the nitrogen compounds and the phosphorus compounds present in the biomass, precipitating any urea content together with the nitrogen, phosphorus and optional potassium content of the biomass, and subsequently separating the biomass into a liquid fraction and a fertilizer fraction.

2. A method according to claim 1, c h a r a c t e r i z e d in that the pre-treatment of a fresh biomass comprises the steps of precipitating a fibre fraction, separating the fibre fraction from the liquid fraction, adjusting the pH-value of the fibre fraction, decomposing the fibre fraction by adding microorganisms and/or enzymes to liberate nitrogen bound in the fibres, remixing the biologically decomposed fibre fraction with the liquid fraction, adjusting the pH-value of the biomass thus treated before adding chemicals in the form of a reactive agent in the form of metal ions.

3. A method according to claim 2, c h a r a c t e r i z e d in that the chemically reactive agents furthermore comprise organic or inorganic acids to form urea complexes which are precipitated together with the nitrogen and phoshorus compounds formed.

4. A method according to any of the preceding claims, c h a r a c t e r i z e d in that the chemical reactions are carried out at a pH- value of between 3.5 and 10 and at a temperature of between 10° and 100°.

5. A method according to claim 1, c h a r a c t e r i z e d in that the pre-treatment of the fresh biomass consists of a degasification and a subsequent mechanical filtration, an adjustment of the pH-value of the biomass and an addition of the reactive agents in the form of metal ions and an adjustment with phosphate ions.

6. A method according to claim 4, c h a r a c t e r i z ed in that the pH-adjustment of the biomass is effected in two steps, by effecting an initial adjustment to a pH-value of from 3-5, preferably 3.5, followed by a preheating of the biomass to a temperature in the range of from 40-55ºC, and by effecting a second pH-adjustment by adjusting the pH-value to 8-9.5, preferably about 8.2, followed by the precipitation.

7. A method according to claim 5, c h a r a c t e r i z e d in that the separation into a liquid fraction and a fertilizer fraction is effected by precipitation, and that the precipitated material is further separated by centrifuging, and subsequently that the precipitated material is optionally mixed with the fibre fraction which is mechanically filtered off.

8. A method according to claim 1 and 2, c h a r a c t e r i z e d in that the potassium compound content of the biomass is precipitated by adding chemically reactive agents which react with the potassium compounds present in the biomass, that the potassium fraction is separated and mixed with the nitrogen and phoshorus-containing fertilizer fraction, and that the remaining liquid fraction is discharged directly to a recipient.

9. A method according to any of the preceding claims, c h a r a c t e r i z e d in that the urea content of the pre-treated biomass is precipitated by adding an organic or inorganic acid, preferably oxalic acid, nitric acid or phosphorus acid in connection with metal ions, which reacts with the urea of the biomass to form urea complexes which are subsequently separated from the liquid fraction of the biomass and discharged together with the nitrogen and phoshorus-containing fertilizer fraction.

10. A method according to any of the preceding claims, c h a r a c t e r i z ed in that the nitrogen, phosphorus, potassium and optionally urea complexes are precipitated simultaneously.