UA75605C2 - Method for treating organic waste substrates and device for realizing method - Google Patents

Abstract

The present invention concerns an anaerobic digestion of animal manures, energy crops and similar organic substrates. The process is capable of refining nutrients comprised in the digested biomass to fertilizers of commercial quality. The invention also provides a method for processing animal carcasses or fractions thereof including meal and bone meal etc., with the objective of providing an alternative means for processing the organic waste material of animal origin while at the same time facilitating the production of fertilizers. The biogas and slurry separation system according to the present invention is preferably integrated with the operations of animal husbandries into a total concept in which the internal and external performances of animal husbandries are optimised. The internal performances concern quality aspects related to the management of the animal houses and include industrial hygiene, animal welfare, gaseous and dust emissions and food safety. The external performances concern mainly energy production and emissions to the environment of nutrients and greenhouse gases and the sale of high quality food product.

Description

12. The method according to item 10, which is characterized in that 30. The method according to item 26, which is characterized in that the pH value is more than 11. the organic material additionally contains straw, 13. The method according to item 10, which is characterized in that that fibers or sawdust. the temperature is above 5070. 31. The method according to claim 26, which is characterized in that 14. The method according to claim 10, which is characterized in that the organic material has a fiber content above 1090, the temperature is above 6070. (M/m). 15. The method according to item 10, which is characterized by the fact that 32. The method according to item 26, which is characterized by the fact that the time of performing the ammonia release stage is organic material has a complex carbon content from 2 to 15 days. virgins, which include cellulose and/or hemicellulose, 16. The method according to item 10, which differs in that and/or lignin, more than 1095 (m/m). the execution time of the ammonia release stage is 33. The method according to item 26, which differs in that from 4 to 10 days.

Sao is added in an amount from 2 to 80 g/kg of dry matter - 17. The method according to item 10, which differs in that wines. the time for the stage of ammonia release is 34. The method according to item 26, which differs in that it takes up to 8 days.

Sao is added in an amount from 5 to 60 g/kg of dry matter - 18. The method according to item b, which differs in that wines. the pH level is 8-12, the temperature is 70"0-35. The method according to item 26, which differs in that 80"C, the proportion of liquid to gas is less than 1:400, and the organic material is crushed before its carrying out the stage of ammonia extraction using lime under pressure. is about 7 days. 36. The method according to item 35, which is characterized by the fact that 19. The method according to item 10, which is characterized by the fact that the organic material is crushed by a screw con- the organic material contains a maximum of 5095 (m/m - a fan equipped with a grinding device, weight/ volume) of solid parts. which supplies the organic material to the device ob- 20. The method according to item 10, which is characterized by the fact that the lime under pressure, where the organic material contains a maximum of 30905 (m/m), is heated by steam injection or steam in the lid of the solid parts. around the pressure lime treatment unit, or 21. The method according to item 10, which differs in that it is a combination of both methods. organic material contains a maximum of 10905 (m//m) 37. The method according to item 26, which differs in that solid parts. includes an additional stage of supplying organic ma- 22. The method according to item 10, which is characterized by the fact that the material treated by the lime processing unit, the separated ammonia is absorbed in the column before entering under pressure, to the fermenter for mesophilic fermentation to the storage tank. and/or thermophilic fermentation before isolation- 23. The method according to item 22, which is characterized by the fact that it is made of organic material ammonia. the column contains water or an acid solution. 38. The method according to item 37, which differs in that 24. The method according to item 23, which differs in that the fermentation is performed by bacterial strains. the acid solution is sulfuric acid solution. 39. The method according to claim 37, which is characterized in that 25. The method according to claim 22, which is characterized in that the fermentation is anaerobic fermentation. ammonia, isolated by treatment with lime under pressure 40. The method according to item 37, which differs in that com, are also absorbed in the above-mentioned column per- organic material of animal origin has red entering the storage tank. nitrogen content (M) over 10905 (m//m). 26. The method according to any of paragraphs 1-10, which distinguishes 41. The method according to item 37, which differs in that the stage of processing the organic matter - fermentation is carried out at a temperature of 15 alu with lime under pressure and is carried out at a temperature of "C to preferably less than 65" WITH. from 120"C to 220"C, under pressure from 2 to 20 bar, with 42. The method according to item 37, which is characterized by the fact that by adding an amount of lime sufficient for the fermentation is carried out at a temperature from 25 to 9 to 12, and the execution time "b to preferably less than 55 26. the stage of processing organic material with lime under 43. The method according to item 37, which is characterized by the fact that the pressure is from at least 1 minute to preferably fermentation is performed at a temperature of less than 60 minutes. 35"C to preferably less than 4526. 27. The method according to item 26, which is characterized in that 44. The method according to item 37, which is characterized in that the temperature is from 1807C to 200"C, the fermentation pressure is performed during the time period is from 10 bar to less than 16 bar, the level is from 5 to less than 15 days, the pH is from 10 to 12, and the time of the stage is 45. The method according to claim 37, characterized in that the treatment of the organic material with lime under pressure fermentation is carried out for a period of time of 5 to 10 minutes. from 7 to less than 10 days. 28. The method according to item 26, which is characterized by the fact that 46. The method according to item 8, which is characterized by the fact that the organic material additionally contains litter, the organic material for ensiling contains manure or manure from cattle, pigs or winter crops , such as birds. rye, corn, clover, and, if necessary, 29. The method according to item 26, which differs in that it includes the budding of plants. organic material additionally contains proteins from 47. The method according to any of paragraphs 1 - 10, which is distinguished by the content of prions of encephalitis spongiform encephalitis by the fact that the production of biogas is carried out in cattle or other prions, and in the above-mentioned or more fermenters with the help of micro-data, prions are destroyed at the stage of processing organic organisms, and it includes anaerobic fermentation of raw material with lime under pressure. organic material.

48. The method according to item 47, which is characterized by the fact that 64. The method according to item 62, which is characterized by the fact that the microorganisms are bacteria that produce the above-mentioned electric current enters the important methane and small fractions of carbon dioxide of the commercial electricity supply network . this in comparison with the production of methane during ferme- 65. The method according to any of paragraphs 1-10, which distinguishes organic material. is due to the fact that microorganisms include bacteria 49. The method according to item 47, which differs in that campylobacter, salmonella, yersinia, ascaris, production of biogas is performed in two fermenters by viruses and viroids. by anaerobic bacterial fermentation 66. The method according to any of paragraphs 1-10, which distinguishes organic material, first by fermenting, which additionally includes the stage of fermentation by thermophilic bacteria in the first fermentation of mineral fertilizers containing nitrogen (M) from the menteri, after which thermophilic enzymes are added of organic material, and the above-mentioned organic material prepared for the second fermentation includes stages i) ammonia collection, a separate fermenter, where fermentation of mesophilic organic material is carried out at the extraction stage by bacteria. ammonia, i) absorption of the above-mentioned ammonia in 50. The method according to item 49, which is characterized by the fact that in water or an acidic solution containing sulfur, the conditions of the thermophilic reaction include tempera acid, and i) obtaining nitrogen mineral tour reaction in the range from 457С to 7576. fertilizers. 51. The method according to item 49, which differs in that 67. The method according to any of items 1-10, which differs in that the conditions of the thermophilic reaction include tempering, which additionally includes the reaction stage in the range from 557С to 6070. production of mineral fertilizers containing phosphorus 52. The method according to item 49, which differs in that that (P), from organic material, and the above-mentioned conditions of the mesophilic reaction include the temperature - the preparation includes stages i) supplying liquid ru reaction in the range from 207C to 4576. manure from the biogas fermenter to the first sepa- 53. The method according to item 49, which differs in that the rator, i) separation of the fermented organic conditions of the mesophilic reaction include the temperature of the inorganic material into the solid fraction and reaction temperature in the range from 30"С to 3570. the liquid fraction of the waste water, i) obtaining 54. The method according to item 49 , which differs in that the solid fraction, which contains part of phosphorus, undergoes a thermophilic reaction within 5-15 days in the form of calcium phosphate (Caz(PO»4)g) and organic phosphates, which were initially a suspension in a liquid in 55. The method according to item 49, which is characterized by the fact that the manure, and the above-mentioned solid fraction can be used as a phosphorus fertilizer during a thermophilic reaction within 7-10. days 68. The method according to item 67, which differs in that 56. The method according to item 49, which differs in that the separator is a decanting centrifuge. the mesophilic reaction is carried out within 5-15 days. 69. The method according to item 67, which differs in that 57. The method according to item 49, which differs in that the solid fraction containing phosphorus is dried, the mesophilic reaction is carried out within 7-10 days. for obtaining granulate containing phosphorous 58. The method according to item 49, which differs in that the fertilizer. any possible foaming is reduced and/or 70. The method according to any of paragraphs 67 and 68, which is removed by adding polymers and/or differs in that the waste water obtained from salivary oils and/or one or more salts. at the stage of separation, has nitrogen (M) and phospho- 59. The method according to item 58, which differs in that ru (P) is less than 0.190 (m//m). that vegetable oil is rapeseed oil. 71. The method according to p. 70, which differs in that 60. The method according to p. 47, which differs in that the spent water is fed to the extractive- the desired flocculation of substances and particles during the reservoir and is reused for the isolation- production of biogas reaches by adding ammonia ions from organic material in the mined calcium, able to create calcium bridges between the reservoirs. organic and inorganic substances in solution 72. The method according to item 70, which differs in that suspensions, and the above-mentioned calcium mos- waste water is reused for you cause the formation of "flakes" from particles. barn cleaning 61. The method according to p. 60, which is characterized by the fact that 73. The method according to p. 70, which is characterized by the fact that the addition of calcium ions also causes precipitation - the waste water is free from sources capable of orthophosphates, including dissolved (POg3: - to spread zoonoses, veterinary viruses, infectious bacteria, parasites, spongiform prions of cattle and

Saz(POg)", and the precipitated calcium phosphate is other prions. remains preferably in the form of a suspension in liquid 74. The method according to any of the paragraphs. 67 and 68, which is different. 62. The method according to item 60, which is characterized by the fact that ammonia from the above-mentioned waste water, the obtained biogas is fed to a gas engine, in a steam extraction unit. able to produce heat and/or electric 75. The method according to item 74, which is characterized by the fact that the current. the selected ammonia is condensed in a two-phase condenser. 63. The method according to item 62, which differs in that the condenser. the above-mentioned heat is used for heating 76. The method according to item 75, which is characterized by the fact that the lime treatment unit under pressure and/or ammonia is condensed in the first phase in the countercurrent of the chlorinator, and/or the reactor for the release of ammonia, liquefied condensate ammonia and/or one or more biogas reactors, 77. The method according to item 76, which differs in that and/or one or more premises for animals. uncondensed ammonia in the first phase is condensed in the counterflow of the solution from the reverse osmosis phase, the main receiving tank is connected to the unit used for the release of potassium (K) with a depressurized unit for treatment with lime under pressure and processed water obtained from the method according to p. 67. with a gas production tank in such a way that 78. The method according to item 74, which is characterized by the fact that the organic liquid manure could be directed from from the first treatment with lime under pressure and to the tank of the extraction tank. gas extraction. 79. The method according to any of paragraphs 67 and 68, which is removed 83. The device according to item 82, which is distinguished by the fact that it is removed by the fact that it additionally includes a dressing stage, additionally includes a silage tank for storing mineral fertilizers containing potassium (K), extracting energy-intensive /g of cultures. from organic materials, and the aforementioned 84. The device according to item 82, which is characterized by the fact that the production includes i) supplying the liquid fraction additionally includes a tank for collecting liquid waste water with potassium (K) content from the first manure, intended for collecting organic stage of separation to the second stage of separation, iii) liquid manure, where the above-mentioned tank for the separation of residual organic and inorganic early liquid manure is connected to the main compound from the liquid fraction, and ii) receiving liquid by the receiving tank, and the above-mentioned reservoir of concentrate, which contains potassium (K), and the above- a liquid manure collection vessel includes a pump for the mentioned liquid concentrate containing potassium K, pumping of organic liquid manure from the reserve- suitable for use as a potassium liquid manure collection vessel to the main fertilizer. receiving tank for organic liquid 80. The method according to item 79, which differs in that manure. the second stage of separation includes the supply of liquid 85. The device according to item 84, which is characterized in that fractions containing potassium (K) through a microfilter, which additionally includes a room for keeping working with alternating aeration and filtration of domestic animals, in which a tank for collecting spent water, and the above-mentioned aer- of liquid manure is placed below the floor level, which ensures the decomposition of residual organic material and the settling of inorganic sediments. 81. A device for obtaining biogas from anaerobes in such a way that the manure can flow from the applied fermentation of treated animal housing to the tank for organic material, which includes solid and collection of liquid manure by gravity. liquid fraction, where the aforementioned 86. The device according to item 81, which is characterized in that the device includes: additionally includes a mixing tank for i) a unit for treatment with lime under pressure for mixing organic material, processed hydrolyzing organic material, with lime under pressure, and organic liquid manure with i) a gas extraction tank for extracting ami-receiving tank, and the above-mentioned tank is made of the above-mentioned organic material, the processing tank is connected with the above-mentioned lime under pressure, and the tank is a given unit for treatment with lime under pressure, extraction of gas is combined with the absorption and the above-mentioned organic material, processed by the column for absorption and condensation of lime under pressure, and organic liquid ammonia manure, must be directed to the mixing tank) fermenter for anaerobic fermentation and from the unit for treatment with lime under pressure, the above-mentioned treated with lime under pressure and above the mentioned mixing tank of organic material, from which ami was isolated, is also connected to the ak extraction tank, and the above-mentioned fermentation in resul- gas. tati ensures the production of biogas, 87. The device according to item 86, which is characterized in that the unit for treatment with lime under pressure additionally includes a device for adding lime, and the gas extraction tank is the above-mentioned device for adding combined in such a way that the organic mother - lime is connected by means of a pipeline to al, treated with lime under the unit for processing with lime under pressure and pressure could be directed from the unit for framing by the tank in such a way that the lime with pressure under pressure to the pno could be directed to the unit for gas extraction tank, and the extraction tank with lime under pressure and to the gas mixing reserve and the biogas fermenter are connected. we in such a way that treated with lime under pressure 88. The device according to item 87, which is characterized by the fact that the organic material from which it was separated additionally includes a grinder for grinding ammonia, could be directed from the reservoir of extracting organic material, and the above-mentioned of gas to the biogas fermenter, the shredder is connected to the mixing rese- and the unit for treatment with lime under pressure by a rvoire and to the gas extraction tank so that the gas extraction tank is also connected so that the mixture of organic material, processed in such a way that the separated ammonia could be cast lime under pressure, and the organic liquid directed from the unit for treatment with lime under manure could be directed from the mixing re- pressure to the gas extraction tank and fed reservoir to the gas extraction tank. to the absorption column. 89. The device according to p. 88, which differs in that 82. The device according to p. 81, which is different in that it additionally includes a main receiving tank - additionally includes a main receiving tank for organic liquid manure, and above - a reservoir for organic of liquid manure, where the above-mentioned main receiving tank is used

combined with a unit for processing with lime under pressure directed to an absorption column for extraction, with a gas extraction tank and from ammonia change. 97. The device according to item 81, which is characterized by the fact that the night liquid manure could be directed from the main- additionally includes a tank for storing amigo receiving tank to the unit for the battery, allocated in the extraction tank gas and processing with lime under pressure, an extraction tank condensed in an absorption column for gas extraction and a mixing tank. of ammonia, and the above-mentioned tank 90. The device according to item 89, which is characterized by the fact that it is connected to an absorption column for storage, additionally includes a tank for collecting liquid column for ammonia extraction in such a way that manure, intended for collecting organic condensed ammonia could be directed from the absorbed liquid manure, and the above-mentioned tank of the friction column for extracting ammonia to the reserve for collecting liquid manure is connected to the header for storing the separated ammonia. by the receiving tank, and the aforementioned 98. The device according to item 81, which is characterized by the fact that the tank for collecting liquid manure additionally includes an air filter for filt- a pump for pumping organic liquid manure of air from the absorption column for extracting from the tank for collecting liquid manure to lead ammonia, and the above-mentioned air filter receiving tank for organic matter is connected to the absorption column for additional liquid manure. 91. The device according to item 90, which is characterized by the fact that the column for extracting ammonia could additionally include a holding room directed to the air filter. domestic animals, in which the tank for collecting 99. The device according to item 81, which is characterized by the fact that the liquid manure is placed below the floor level, additionally includes a tank for liquid biomass of the premises for keeping animals and is connected to the storage of liquid biomass, and the aforementioned the above-mentioned room for keeping twa- this tank for liquid biomass is a combined rin in such a way that the manure can come with impur- with the biogas fermenter and with the extraction tank for keeping animals to the gas tank in such a way that the liquid biomass can be collected liquid manure by gravity. can be directed from the tank for liquid bio- 92. The device according to item 81, which differs in that the mass to the biogas fermenter and to the tank additionally includes a device for adding lime, extracting gas. and the aforementioned device for adding 100. The device according to item 81, which is characterized by the fact that the lime is connected to the unit for processing with additionally includes a tank for organic acid-lime under pressure so that the lime can be used to adjust the pH of the organic material in the directed to the unit for processing with vap- biogas fermenter, and the aforementioned nom under pressure. the tank for organic acids is connected to 93. The device according to item 81, which is characterized by the fact that the biogas fermenter in such a way that the organic acid can be directed from the tank to homogenization for feeding and homogenization organic acid to biogas fermenting organic material, and the aforementioned. The feeding-homogenization device includes 101. The device according to claim 81, which is characterized in that screw conveyors and a built-in shredder, and additionally includes a buffer tank for the above-mentioned feeding-homogenization device is to give PAX, and the above-mentioned buffer is connected to the unit for processing with lime under the tank is connected to the biogas fermenter pressure so that the homogenized solid rum so that the fermented and degassed organic material could be directed to the aggre organic material could be directed from the ghat for treatment with lime under pressure. biogas fermenter to the buffer tank 94. The device according to item 93, which differs in that the additionally includes a reception station for receiving 102. The device according to item 101, which differs in that the collection of solid organic material, and that additionally includes a decanting centrifuge, the reception station is equipped with screw con- for the separation of fermented and degassed orvairs in the floor, and the station reception of organic material into a semi-solid fraction, which with a lime processing unit under pressure includes phosphorus, and an aqueous phase, and above the feeding-homogenization system in this way, the mentioned decanting centrifuge is combined with so that the solid organic material is homogenized buffer tank, so that the buffer could be directed from the receiving station through the fermented and degassed organic feed-homogenization system to the unit for the material could be directed from the buffer rese- processing with lime under pressure. rvoir to the decanting centrifuge. 95. The device according to claim 94, which is characterized in that 103. The device according to claim 102, which is characterized in that it further includes a scale for weighing a solid which further includes a tank for collecting organic material. semi-solid fraction, which includes phosphorus, after 96. The device according to item 81, which is characterized by the fact that decanting centrifugation, and above additionally includes a tank of sulfuric acid, said tank for collecting semi-solid for storage of sulfuric acid, and above- fraction, which includes phosphorus , is connected to the de- mentioned tank of sulfuric acid is connected to the decanting centrifuge in such a way that the semi- with the absorption column for the production of ammonia, the solid fraction, which includes phosphorus, could be in such a way that the sulfuric acid could be directed from the decanting centrifuge to the reserve

ware for collecting the semi-solid fraction, which 112. The device according to item 109, which is characterized by the fact that it includes phosphorus. which additionally includes the installation of a reverse os- 104. The device according to item 102, which is characterized by the fact that it additionally includes a second buffer reserve - a tank for waste water, and ar for buffering the aqueous phase after decantation - the above-mentioned installation of the reverse osmosis is a rest of centrifugation, and the aforementioned buffer tank is connected to the above-mentioned tank for the above-mentioned water phase after the decanting centrifuge, the waste water could be directed from the decanting moss to the reverse recovery unit. centrifuges to the second buffer tank. 113. The device according to item 112, which is characterized by the fact that, 105. The device according to item 104, which is characterized by the fact that it additionally includes a tank for collecting that additionally includes a room for holding dissolved K, and the above-mentioned reservoir of domestic animals, and the above-mentioned second tank for collecting of dissolved K is connected to the installation, the buffer tank is connected to the room of the reverse osmosis unit in such a way that the water from the second buffer tank could be directed to the tank for collection should be directed to a room for keeping dissolved K. animals. 114. The device according to item 81, which differs in that 106. The device according to item 104 and 105, which differs- additionally includes a unit for condensation of the axis in that the above-mentioned second buffer reserve in the above-mentioned biogas formed through the voire is connected to the production tank anaerobic fermentation of organic material, gas in such a way that the buffered water from the second and the above-mentioned installation for the condensation of the buffer tank could be directed to the water is connected to the biogas fermenter such a gas extraction tank. in such a way that the biogas formed through anaerobic 107. The device according to item 104, which differs in that fermentation in a fermenter, could be directed, which additionally includes a steam stripper for the desorption of the biogas fermenter to the unit for the combustion of the remaining ammonia, with water phase, water densification. from a decanting centrifuge, and above- 115. The device according to item 114, which differs in that the mentioned steam stripper is connected to the second, which additionally includes a gas storage for storage - a buffer tank in such a way that the buffer of biogas formed through anaerobic fermentation - dug water from the second buffer tank for the extraction of organic material, and the above-mentioned one should be directed to the steam stripper. not the gas storage is connected to the installation for 108. The device according to item 104, which is characterized in that the condensation of water in such a way that the biogas can be that the aforementioned steam stripper is connected to directed from the installation for condensing water to the absorption column for the production of ammonia and- gas storage. 116. The device according to item 115, which differs from the above-mentioned steam stripper, could be sent to the above-mentioned absorption column for cleaning biogas from trace amounts of sulfur extraction of ammonia. hydrogen present in the processed biogas, pri- 109. The device according to paragraphs 104 and 107, which is distinguished by the fact that the above-mentioned gas treatment plant additionally includes a tank for the gas storage decoupled in such a way that the processed water for collecting water, produced biogas can be directed from the gas storage to for ammonia in the above-mentioned steam strippers, and gas cleaning plant. for collecting buffered water from the above-mentioned 117. The device according to item 116, which differs from that of the second buffer tank, and the above-mentioned additionally includes a combined plant with a given tank for waste water is a combination of heat and energy for burning the above-mentioned with the aforementioned steam stripper and from the aforementioned biogas and power generation and the aforementioned second heat buffer tank, and the aforementioned combined plant in such a way that the water from the aforementioned steam from the heat and power generation is connected to the stripper and the buffered water from the aforementioned aforesaid gas treatment plant, thus, the second buffer tank could be designed so that the above-mentioned purified gas could be directed to the waste water tank. directed from the above-mentioned gas treatment plant 110. The device according to item 109, which differs in that the installation to the above-mentioned combined plant additionally includes a room for keeping heat and energy production. domestic animals, and the above-mentioned reserve- 118. The device according to item 81, which differs in that the ar for waste water is connected with a room for keeping animals in such a way, them) a room for keeping domestic animals, so that the waste water can be directed, and organic liquid manure can come from the premises for keeping animals. premises for keeping animals to the unit for 111. The device according to paragraphs 109 and 110, which differs - treatment with lime under pressure and/or to the tank by the fact that the above-mentioned tank for the production of gas, soda water is connected to the tank (the tank for collecting ammonia, which was the release of gas) , in such a way that the spent oil was produced in the gas production tank, and the water could be directed to the production tank, the ammonia collection tank and the gas release tank. gas production are connected in such a way that the released ammonia can be directed from the pressure lime treatment tank and/or to the gas production tank to the tank for collecting gas production, ammonia, m) silage tank for obtaining silage m) silage tank for content of fermented plant material containing energy-intensive organic material in the form of silage, culture, m) fermentation tank of previous m) fermentation tank of preliminary anaerobic fermentation for anaerobic work for fermentation of silage and/or organic fermentation of silage for removing biogas from blue of the material treated with lime under pressure in the loess, and the fermentation tank is under mesophilic or thermophilic conditions, and the ordinary anaerobic fermentation is connected with the pre-treatment fermentation tank with the silage tank, so that it is connected with the silage tank and the aggregate silo could be directed from the silage reserve - volume for treatment with lime under pressure in such a way, ara to the fermentation tank before the silage or treated with lime under pressure of small anaerobic fermentation, and the fermenting material could be directed from the silage reserve tank of the previous anaerobic voire or unit for treatment with lime under pressure, the fermentation is also connected with the gas tank to the fermentation tank of gas production in such a way that the fermenter of the pre-anaerobic fermentation, and the fermenter silo could be directed from the fermentation tank of the pre-anaerobic tank of the pre-anaerobic armed fermentation is also combined with reserving to the gas production tank, gas production aromas in such a way that mii) a decanting centrifuge for separating fermented silage or organic material, solid and liquid fractions, and the decanter is treated with lime under pressure, could be directed- the centrifuge is combined with biogas enzyme from the fermentation tank before anaerobic fermentation of the above-mentioned anaerobic fermentation to the tank treated with lime under pressure of organic ma- gas production, terial from which ammonia was isolated, thus mi) a decanting centrifuge in which fermented to fermented treated with lime under pressure, the organic material obtained as a result of the organic material from which ammonia was separated from aerobic fermentation in the biogas fermenter could be directed from the biogas fermenter to the waste water and solid fracter to the decanting centrifuge, which (contains organic and inorganic matter) a tank for collecting the semi-solid fraction, al, including P (phosphorus), and the decanter containing more than 5095 (ml) of phosphorus, the resulting centrifuge is connected to a biogas fermenter - after decanting centrifugation, and the rum for anaerobic fermentation above-mentioned - collection tank and decanting centrifuge - processing cast with lime under the pressure of an organic mag are connected in such a way that the material from which ammonia was separated, thus phosphorus could be directed from the decanting to be fermented treated with lime under pressure centrifuges to the tank for collecting the semi-organic the material from which the solid fraction, which includes phosphorus and ammonia, was separated, could be directed from the biogas fermenter- x) tank for waste water for the primer to the decanting centrifuge, collecting the liquid fraction in the form of waste water, mii) ceramic microfilter for separation of the remaining solid materials obtained as a result of the decanting centrifuge from the waste water, dressing, and the tank for the spent rye as a result of the decanting centrifuge water and the decanting centrifuge are connected, and the ceramic microfilter is connected in such a way that the waste water can be with decanting centrifuge in such a way that it is directed from the decanting centrifuge to the res er - waste water obtained by decanting - a waste water decanter. which centrifugation, could be directed to 119. The device according to item 118, which is characterized by a ceramic microfilter, and which additionally includes a gas engine, and their) tank for collecting biogas, and the rese- gas engine and biogas fermenter is a spolur- reservoir is connected to the biogas fermenter, so that the biogas could be sent from the biogas fermenter to the gas fermentation of the lime-treated pressurized organ. of night material, from which ammonia was isolated, could 120. The device according to item 81, which differs in that it is directed from the biogas fermenter to the device additionally includes a collection tank, and the above-mentioned reserve- a room for keeping domestic animals, ar for collecting of biogas is connected to the release, and the premises for keeping animals include for the distribution of biogas or connected to the gas tea a) cleaning system with the use of a cleaning engine. of water for cleaning channels for manure 121. The device according to item 81, which is characterized by the fact that for keeping animals, B) ventilation of the above-mentioned absorption column for extracting channels and c) a transport system for trans-ammonia is connected to a tank of sulfur the transport of manure, which includes organic matter in such a way that sulfuric acid can be al, from the room for keeping animals to the unit, is directed to the absorption column for extractant for treatment with lime under pressure and/or to ammonia, of the gas production tank so that the absorption column for ammonia production is com- organic liquid manure could be directed with attached with the tank for the storage of the dedicated space for keeping animals to the unit for ammonia so that the condensed ammonia could be directed to the tank for storage treatment with lime under pressure using a system- separated ammonia and could be stored in the above- mentioned serving-homogenization for serving and the tank for the storage of separated ammonia, the mogenization of solid organic material from the above-mentioned tank for storing the condensation of receiving to the unit for the treatment of waxed ammonia has an outlet for the removal of compressed ammonia, and the above-mentioned feeding device - the aforementioned absorption column for extracting homogenization includes screw conveyors and a built-in ammonia tank is connected to the above-mentioned tank, a shredder, gas extraction, and the above-mentioned additional device- a tank for liquid biomass for storing liquid includes biomass, and the above-mentioned tank for a room for keeping domestic animals , of liquid biomass is connected to a biogas fermenter - a tank for collecting liquid manure, a device and a gas extraction tank for collecting organic liquid manure with admixtures so that liquid biomass can be directed from the premises for keeping animals, a tank for liquid biomass to biogas fuel - and the tank for collecting liquid manure is a rmenter and from the tank for liquid biomass to the room for the reservoir of gas extraction, keeping animals and connected to the above-mentioned tank for organic acid for regulating the room for keeping animals, located below the floor level in such a way that the pH of organic material in the biogas fermenter so that the manure can come from the room for the utrine, and the above-mentioned tank for animal organization to the tank for collecting liquid night acids is connected to the biogas manure by gravity, and the fermenter in such a way that the organic acid tank for collecting of liquid manure could be directed to the biogas fermenter, a pump for pumping organic liquid manure, from a tank for collecting liquid manure by a decanting centrifuge for separation of enzyme-combination with the main receiving tank of organic liquid manure and degassed organic material, and the above-mentioned semi-solid fra cation, which includes phosphorus, and the main receiving tank is also the aqueous phase, connected to the unit for processing with lime under and the above-mentioned decanting centrifuge is pressure, the gas extraction tank, silage connected to the fermenter with the help of a buffer tank for obtaining silage vegetable tank for adding PAH in such a way that the material containing the energy-intensive cultures and that the degassed and fermented organic material by the mixing tank can be directed from the biogas ferment material treated with lime under pressure to the buffer tank, and thus organic liquid manure, and the above-mentioned - so that the buffered organic material could be the mixing tank is connected to the - directed from the buffer tank to the decant- the mentioned unit for processing with lime under the throttling centrifuge, pressure, and the above-mentioned buffer tank the aforementioned organic material treated includes a pump for removing the above-mentioned lime under pressure, and organic liquid manure of digested and degassed organic matter to the mixing tank from the unit from the above-mentioned buffer tank to the coil for treatment with lime under pressure and the main above-mentioned decanting centrifuge, and the receiving tank, and the mixing of the above-mentioned decanting centrifuge is connected to the tank is also connected to the tank for collecting semi-solid gas production through a chopper for the crushed fraction that includes phosphorus, separated from the organic material in such a way that the mixture of the above-mentioned aqueous phase in the decanting center - of organic material treated with lime under the fuze in such a way that the semi-solid fraction could by pressure, and organic liquid manure could be directed to the above-mentioned tank crushed and directed from the mixing tank - to collect the semi-solid fraction, which includes ra to mining tank of gas, phosphorus, and the main receiving tank includes a gas storage for storing biogas formed and a pump for pumping organic liquid during anaerobic fermentation of organic matter from the main receiving tank to the rial, a unit for processing with lime under pressure and/or the aforementioned the gas storage is connected to the gas extraction and/or mixing tank with the above-mentioned fermenter in such a way that the tank, biogas formed through anaerobic fermentation lime addition device, which includes a tru- in the fermenter, could be directed to the storage pipeline for supplying lime to the unit for of gas by passing through a unit for condensing - treatment with lime under pressure or mixing sation of water in the above-mentioned biogas formed by a tank, a scale for weighing solid organic - through anaerobic fermentation, and the above material, a silo tank for receiving - the mentioned unit for condensing water is use of silage plant materials ial, which contains a biogas fermenter and gas storage, burns energy-intensive crops, so that the biogas can be directed from a receiving station for receiving solid organic biogas fermenter to a facility for condensate material, and the receiving station is sation of water and further to the gas storage, equipped with screw conveyors in the floor, and the aforementioned condensing unit, the receiving station is connected to the water unit, has an outlet installed in such a way that the condensed water from the biogas can be removed obtained from the decanting centrifuge, could be from the device, a gas treatment plant for the purification of biogas from trace amounts of hydrogen sulfide, the occurrence of gas and the above-mentioned room for the presence of treated biogas, before incineration, animal keeping, treatment of the above-mentioned biogas, a tank for waste water for collection, and the above-mentioned water gas purification plant , desorbed for ammonia in the above-mentioned is connected to the above-mentioned gas storage tapar stripper, and to collect water from the above, so that the biogas can be directed from the above-mentioned decanting centrifuge through the above-mentioned gas storage directly to the above-mentioned gasification of water through the above-mentioned second buffer treatment plant, tank, combined heat and power plant, and the above-mentioned tank for burning the above-mentioned biogas, water is connected to the above-mentioned steam and the above-mentioned combined plant with an extractor in such a way that the above-mentioned water, heat and energy production is combined with the above-desorbed for ammonia, could be directed with the mentioned gas purification plant of the above-mentioned steam stripper in such a way that the above-mentioned purified biogas could be used water tank, and be directed from the above-mentioned gas treatment- the above-mentioned waste water tank to the the aforementioned of the combined plant is connected to the above-mentioned second buffer plant for the production of heat and energy, a tank in such a way that the above-mentioned buffer plant with of the above-mentioned biogas is produced by the electric mentioned second buffer tank to the above-mentioned, which can be directed to the commercial waste water tank, and the electricity supply network, and the above-mentioned spa- the above-mentioned waste water tank biogas also produces heat, which can be combined with the gas extraction tank and using the above-mentioned animal housing by way of cooling, this combined heat production plant in such a way that the waste water from the water circuit energy recovery tank and the subsequent used water could be directed to the above-mentioned warm, absorbed in the above-mentioned gas production tank and the above-mentioned water circuit for heating the aggre- mentioned room for keeping animals, a ghat for treatment with lime under pressure, a tank, a reverse osmosis installation for separating potassium, gas production, a fermenter and/or a room from waste water a tank for washing animals, a steam stripper for dissociated water, and the installation of reverse sorption of the remaining ammonia from the aqueous phase, odemos includes a) a ceramic microfilter and b) rye from a decanting centrifuge, a reverse osmosis filter for filtering the above-mentioned steam stripper includes dissolved substance obtained as a result of ceramic- steam-water heat exchanger that is heated, constant microfiltration, and filtering forms using electricity and/or heat, produced potassium concentrate, bleni in the above-mentioned combined plant with and the aforementioned installation of reverse osmosis for heat and energy production, and su is connected to the above-mentioned tank for the above-mentioned steam stripper is connected to the waste water in such a way that the waste water can be directed from the tank in such a way that the above-mentioned aqueous phase obtained from the waste water to the above-mentioned decanting centrifuge , could be directed to the reverse osmosis, and to the above-mentioned steam stripper, and the above-mentioned reverse osmosis installation is the above-mentioned steam stripper is connected to the tank for collecting dissolved by the absorption column for the extraction of ammonia and K in such a way that the potassium concentrate from the installation in such a way that the above-mentioned separated ammonia, reverse osmosis could be directed to the above-desorbed in the above-mentioned steam strip- mentioned tank for collecting dissolved ri, could be directed to the above-mentioned absorption column for the extraction of ammonia, and the above-mentioned reverse osmosis installation has the aforementioned decant ing centrifuge and the above-mentioned release for the solute from the osmosis filter, this steam stripper is connected with the help of such a way that the dissolved substance can be go of the second buffer tank, removed from the device, and the above-mentioned second buffer reserve- and the above-mentioned tank for collecting ar is combined with a decanting centrifuge and from the dissolved K has an outlet for the above-mentioned conpar stripper in such a way that the aqueous phase, potassium concentrate in such a way that the K-solution could be obtained in the decanting centrifuge, could be taken out with the device. directed from the decanting centrifuge to the second 122. The device according to any of paragraphs. 81-121, which from the buffer tank, and in such a way that the buffer tank differs in that the unit for treatment with lime, the quarried water phase could be directed with a drup- under pressure consists of two elongated tubular buffer tank to the steam stripper, similar horizontal chambers with a central, and the above-mentioned second buffer tank, and the chambers are fixed one on the ar is also connected to the extraction tank. gas and with a room for keeping animals 123. The device according to item 122, which is characterized in that the above-mentioned buffered water, which is a feeding and homogenizing device for homogenization

genization and feeding of homogenized organic- 133. Device according to any of paragraphs 120 and 121, which material, which includes solid particles, differs in that the dissolved substance of the unit for processing with lime under pressure includes screw conveyors used for washing drain channels and a built-in shredder. who manure systems of premises for animals. 124. The device according to item 123, which differs from that, 134. The device according to any of items 81-133, which since the device for adding lime is combined with differs in that the organic material includes the upper chamber of the unit for processing with lime at least one of the plant materials to which under pressure, and the lower chamber of the unit for processing with corn, energy-intensive agricultural crops, with lime under pressure is combined with the mixing water and/or the remains of agricultural crops. tank, which is also connected to the receiver 135. The device according to any of paragraphs 81-133, which is a separate tank for receiving organic material, differs in that the organic material includes liquid manure, and the mixing tank is animal carcasses or their parts. used for mixing organic mater- 136. Device according to any of paragraphs 81-133, which differs from organic waste treated with lime under pressure in that organic material includes liquid manure directed to the mixing process of slaughterhouse waste. reservoir from the receiving tank. 137. The device according to any of paragraphs 81-133, which is 125. The device according to any of paragraphs 96-114, which differs in that the organic material includes meat and bone meal. Ammonia extraction includes a two-phase gas purifier 138. The device according to any of paragraphs 81-133, which is a single condenser in which ammonia initially differs in that the organic material includes condenses in the countercurrent of the cooled condensate- blood plasma. that ammonia, and ammonia gas, not condensed on the first 139. Device according to any of paragraphs. 81-133, which from the condensation stage, condenses in the second stage differs in that the organic material includes water countercurrents. risky and non-risky material in view of 126. The device according to item 125, which differs in that the presence of bovine spongiform prions or other reasons why sulfuric acid is added to the return flow. water in the second stage. 140. The device according to any of paragraphs 81-133, which re- 127. The device according to item 126, which differs in that the organic material includes that the final ammonia concentrate contains ammonia in the organic material of animal origin, which concentration is more than 25905 (m/m). has a nitrogen content (M) of more than 1095 (m//m). 128. The device according to any of paragraphs 118-120, which is 141. The device according to any of paragraphs 81-133, which is distinguished by the fact that the fermentation tank differs in that the organic material has a content of preliminary anaerobic fermentation is a reserve of complex carbohydrates containing cellulose and/or a thermophilic fermentation vessel. hemicellulose, and/or lignin, for example, more than 10905 129. Device according to any of paragraphs 118-120, which is (mm). is distinguished by the fact that the fermentation tank 142. The device according to any of paragraphs 81-133, which is a reserve from previous anaerobic fermentation, differs in that the organic material includes the ware of mesophilic fermentation. more than 5095 (m/Li) of cellulose and/or hemicellulose, 130. Device according to any of paragraphs 81-129, which is od- and/or lignin per dry weight of organic material. differs in that biogas mainly includes 143. The device according to any of paragraphs 81-133, which is marked. differs in that the organic material includes 131. The device according to any of paragraphs 120 and 121, which is manure and its liquid biomass. characterized in that the ceramic microfilter 144. The device according to claim 143, which is characterized in that it removes particles larger than 0.01 μm (micron), from which manure is obtained from cattle, pigs or poultry. waste water. 145. The device according to any of paragraphs 81-133, which is 132. The device according to any of paragraphs 120 and 121, which differs in that the organic material includes differs in that the potassium concentrate will be obtained as livestock bedding. from waste water by using 146. The device according to any of paragraphs 81-133, which from the energy produced by the gas engine is heated by the fact that the organic material includes waste water obtained in the resulting silage crops. those of decanting centrifugation, and heating 147. The device according to any of paragraphs 81-133, which gives off a distillate that contains differs in that the organic material includes a potassium concentrate. beets, corn and clover.

First of all, this invention concerns anaerobically integrated with livestock enterprises in the processing of animal organic fertilizer, a single system in which internal and agricultural crops and similar organ-external aspects of animal husbandry are optimized. substances This process is capable of converting One of the additional aspects of the invention is the possible nutrients contained in the processed left its application for the elimination of biomass waste into fertilizers of commercial quality. Animal system in the form of animal carcasses, slaughterhouse waste, production of biogas and separation of liquid manure from coarse ground meat and bone meal, etc. However, with this invention, in the optimal version, the crops are processed at the plant into fertilizers,

seeds for their use in agriculture. 721-726.

Is it possible to contain prions in encephalitic spongiform encephalitis? K. of cattle (Cattle) or other prions (1995) Attopia z(pPrripa. is significantly reduced or completely eliminated by this hyskehypatsvigye 120, 960-969. process. Livestock production by this process - Spasyk A., 7agluski K., apa Isiek 9. (1994) Catfish is not used as feed, but as fertilizer.

Destruction of possible prions of spongiform encephalitis viirripd soimtp5 g hetoma! oyi attopia iot

Cattle in biomass processed at the plant in poedsopaepzaiyev. 2isKegipaivine 119, nanni with the use of processed biomass as 1008-1015. fertilizers instead of being used as feed significantly Spetspd K. S., Spi YII M., apa M/opd M. N. (1997) significantly reduces if not eliminates the risk of infection of animals Attopia 5igirripd az a rge- or humans with prions of encephalitis spongiform cattle igeaitepi og Iapaii Ieasnaitei . UMaieg Aig apa 5oiyi or their modified forms. Research 94,209-221.

Internal aspects include aspects of quality, Mao, R.N., Spep, A., apa Go, K.M. (1995) Ketomai oi related to the maintenance of a livestock farm, and pygodep ygot vmipe tapyge include industrial hygiene, animal husbandry, mzhaviemzhaisegtv ru attopia viyrripud. Viotesppoiodu « control of gas and dust emissions and the safety of Arriiea Misgorioiodu 54,17-20. fodder External aspects concern, mainly Alkaline and thermal hydrolysis, energy production and control of thermal pre-treatment of biomass before releasing nutrients into the environment by anaerobic fermentation - this is a detailed description of and greenhouse gases and sale of high-quality technology in the literature, for example: Lee and Neuke of food products, as well as alternative (1992). In recent years, the previous thermal method of liquidating animal corpses, etc. urban waste processing also uses

Release of ammonia was on an industrial and commercial scale

The chemistry of ammonia is well known and the release of ammonia from mine Satri A5, Billingstad, Norway different liquids is a well-known technological Wang et al (1997a and B) discovered that the process. It is used, for example, in sugar-day thermal treatment of municipal waste at 60" S. industry (Bunert et al., 1995; Chakuk and and duration of hydraulic treatment of wastewater on others, 1994; Benito and Cubero, 1996) and municipal sewage treatment plant 8 days gave an increase by producers to treat landfills (Cheung et al., tva of methane at 52.195. A similar result was 1997). Ammonia can also be extracted from pig was obtained by Tanaka et al. (1997), however, single manure using the same technology with alkaline hydrolysis gave the most successful process, as in industry (Liao et al., gas release (200905). McCarthy et al. 1995). performed a number of studies that proved that the

As the basic principle of large-scale pre-thermal and alkaline hydrolysis significantly increases the occurrence of ammonia, an increase in pH and aeration and gas production are taken. However, the pH should be approx. heating of sewage or liquid manure. To increase the pH from 10 to 12, optimally 11 or less, CaS(OnH)" or CaO are often used. above, before chemical hydrolysis provides significant

However, other alkalis can also be used, for example: effective additional gas production.

Mahon or KOH. However, on an industrial scale The results of research by Wang et al. (1997) use lime, for example, in production suggest that the standard values of paramet- cement, and therefore it is cheap and easy to purchase ammonia production ditch according to section 2.1 (pH close to wholesale. 10-12, ideally 11 or more, and

Where the separated ammonia is absorbed and the boiling temperature is about 707 C or higher during the ammonia concentrate is poured into the absorption tubes (weeks) will increase the gas yield. sulfuric acid is used. Sulfuric acid Reference: lota is a common industrial substance, it is Gi M. HU., apa Moike T. (1992) Ordgadipdoi apaegobis is sold in a quality suitable for use in didesiop oi mausie asiimayetei ziydde ru Sheptai rge- absorption columns for extraction ammonia from rhyd- igeaitepi. Uaieg Zsieepse apa Tesppoiodu 26, 3-4. who manure and other sewage (for example: Sakuk MesSapu R. I, Moipd I U., Sbozzey 9). M., Zishskeu 0. and others, 1994). S, apa Nea/uu g, u. V. Neai igeaitepi g ipsgeavzipd

Based on the experience accumulated in the sugar teiShape uieiy ybot ogdapis taiegia!v. (aptoga of industry, it was established that the most suitable parameter values are: temperature 70" Tapaka 5., Korauavni T. Katiuata K. apa Viidap M.

WITH; pH in the range of approximately 10 - 12; and the number of I. M. 5. (1997) ENesibv oi Shepto sPpetisa! rge- liquid gas 1:800, 9695 efficiency. іSheaitepi op She apaegoris aidevip oi mavie

For the production of ammonia from liquid manure, install asiimaiei zishdde. In the case of Zsiepse apa Tesppoiodu Z5, it was found that the optimal values of the parameters are 209-215. at low temperature there are: temperature 227"C; pH Mapd 0., Modisni S, Naga U., Zpagop S, KaKitoiyu approximately 10-12; quantity of liquid gas 1:2000, 9095 K., apa Kayu U. (1997a) Zschshaiye5 op apaeegobis efficiency, 150g of work (Liaotaiinsi, 1995).

Reference: Iietregashte op Biodedgadayop oi mavie asiimagey

Vepyo b. b. apa Syrego M. T. b. (1996) Attopia will be released. Epmigoptepia! Thesppoiodu 18, 999-1008. eiiitipayop iot Bbeeei zidag Muapd O., Modispi S. Ku Kypipobi M., Naga U.,

Tiasogu sopdepzaie zpeat5e bu a z(yrripo- Kakito K. Odazha N. I. Apa Katyu U. (1997B) gearzogbipdu zuziet. 2isKegipaiviye 121, IpYamepse oi Ppuagashis hesepiop te op apaegobis aidesiop o oi rge-neavy v5ishdde. Viostesppoiodu kiv

Tesppidiez 11,105-108. From examples of the use of decanting

Sanitary treatment of centrifuges in recent years can be brought to the plant

Sanitary treatment of liquid manure in front of "Momo Mogaizk" in Kalundborg, where all waste of large insulin-fermenting aggregates are processed by transport and application in the field is an important measure to reduce the risk of the spread of gats. With the help of decanting centrifuges, obesozoonosis (diseases transmitted to humans from urban sewage sludge (Aga I amai rin) and veterinary viruses, bacteria and parasites A/5 is also produced). Decanting centrifuges separate dry (for example: Bendiksen, 1999). Anaerobic digester) matter from sediment or waste, and water bathing has proven to be effective in reducing the component of wastewater is discharged to the usual amount of zoonoses in liquid manure, but did not destroy treatment plants. facilities for wastewater treatment. these organisms are whole (Bendiksen, 1999; Pagilla and Cattle Liquid Manure Separation Study, others, 2000). The use of CaO for sanitary pigs and degassed manure proved that, on the treatment of sewage sludge also proved, first, decanting centrifuges are able to process the number of roundworm eggs and parasites (Eriksen vati all organic fertilizers without any problems and others, 1996) and viruses was significantly reduced, but it was also found that centrifuges were removed to zero (Turner and Burton, 1997). about 70905 dry matter, 60-809o total

Reference: foot P and only 1495 of the total M from liquid manure,

Vepaikhep N. 9. Nudiepis zatesu - gevyiv oi vsiepiyis pre-fermented by a thermobattery (Moller ipleziyidayope ip Oeptaik (zapigayop gedspigetepiv ip and others, 1999; Moller, 2000a). Corresponding values

OBapizpy Biodav riapibye). Nopeppeiteg betipag IEA of primary liquid manure from cattle and pigs were

Vio-epegdu UMogk5Ppor Magsp 1999. somewhat lower. It should be noted that from the waste

Egpikzep GI, Apagezep R. IIzoe V. (1996) Ipasiimayop is recommended only 14595 of the total M. og Avsaigiz zisht edd5 ashgipd viogade ip Ііite igeasey Calculation of the total cost of processing gave 5 vzemzhade 5ishyde. MUMageg ANezeagsy 30,1026-1029. DKK/m3 of manure with a manure volume of 20,000 tons

Radia K. A., Keith N., apa Spetzprat T. (2000) or more. If the volume of manure exceeds 20,000

Aegobis (Sheptoriie apa apaegobis tesoriie (geaitepi ton, decanting centrifuges are justified and de- oi zm/ipe mavivie. UMageg Nezeagsi 34, 2747-2753. sewing equipment for separation of dry matter

Titeg S apa Vypop S. N. (1997) Tpe ipasiimayop oi and general P from liquid manure (Moller et al., migizez ip rid zishpiev: a hemivem/. 1999).

Viogezotsgse Thesppoiodu 61, 9-20. Under normal conditions, it makes no sense to process

Foam you liquid manure with the help of a decanting center

The formation of foam due to anaerobic digestion, since it is not associated with a reduction in o06', can be a serious problem for him or other benefits for farmers. Loss for the use of fermenters. A number of substances for ammonia after the application of treated liquid manure to reduce foaming are freely available in the field soil can be slightly reduced due to including various polymers, vegetable fat- increasing the rate of infiltration into the soil (Our (for example: rapeseed oil) and various salts ller 20005 ), but it provides a much greater incentive (e.g., Vardar-Sukan, 1998). However, polymers for farmers to use decanting centers can cause harm to the environment, in addition, they fugue. often expensive and ineffective. Link:

Reference: MoPeg about N.V. (2000a) Orkopsepigegipd ai

Magaag-5yKap R. (1998) REosatipd: sopzedpepsez, paegipdz5ioPeg and pizaugdodpipd tey rgemepiyop apa aezigisiyop. deKapiegsepipide 09 5Kypiergezb5e. Moiai 12.

Vioyesppoiodou Admapsez 16, 913-948. Zerietreg 2000, EogezKpipdzsepieg Woodpoit.

Flocculation Moieg N. V. (20005) Sode geziiageg tea ai zeragege

Calcium ions are well known as flo-duiPe agents. Mazkipriadei 25. aydyvi 2000. culation of substances and particles due to the formation of MoiPeg N.V., Sypa I., apa Zotteg 5. 5. (1999) Calcium bridges between organic and inorganic edshii zeragayop oi Imeviosk vishtu: eiisiepsu apa substances in solutions or suspensions, forming owls. thus "flakes" of particles (for example, Aga I ama! A/5 SuPezeragegipd. Zeragegipdzgeziaeg

Sanin and Vesilind, 1996). For this reason, calcium tea desapiegsepigcde. used for dewatering sewage sludge Fallout of P into sediment (Higgins and Novak, 1997). Dissolved P precipitates almost immediately after

Reference: addition of Ca in the form of calcium phosphate

Niddip5 M. 9. apa Momak 9. T. (1997). Tne eMesiv Saz(ROz)" (Cheung and others 1995). oi saiop5 op She zeshipd apa de-magsegpo oi asiimaseei Link: published: Iaroghaigu gezitsy5. UMaieg Epmigyuoptepi Specpd K. S., Spy G M., apa Uuopd M. N. (1997)

Veseagsi 69, 215-224. Zapip R. 0., apa Mezviipa R. A. Attopia vii Pirripd az a rgeigeaitepnog Iapanii (1996) Zupipeis ziydde: A rpuzisaspetisa! that way! ip Ieasnaiiye. UMaieg Aig apa 5oi! Royshop 94, 209-221. ipaegviapaiipo bio Possciatsyop. UMaieg Epmioptepi Prevention of struvite formation

Veseagsi 68, 927-933. Another important additional factor is that

Separation of liquid manure by a decanter that precipitates P in combination with separation by a centrifuge, extraction of P ammonia prevents the formation of struvite (MOMNAROZ).

Decanting centrifuges are used in a number of Struvit is an additional operational problem in technological processes during the last 100 heat exchangers, when transporting pipelines

waters, etc. (Kruger 1993). The mechanism is type- Miiysayop ip goiaipo abs vuvzietv-I. Stpepya yug leniya P by the formation of SarRoh, as well as vyda- ShMapeyiop yot ohudep Yu attopia hafe Itkayop. production of ammonia by its separation. Removal of R UMaieg Rezeagsp 19,1119-1127. bsoy u. AND.; Meibop and ammonia prevent the formation of struvite. 0. 9U. Tsi M., apa Voop R.M. (1998) Apa! GPS

Reference: tetbgape Biogeasiog zubiet god eppapsei aeeegobis

Ktydeg (1993) 5igimii aappe!5e and riodaztaeIezapiade. geteaiayop oi podnp-zigepdiy ipaivigai! have

Ktydeg U/asiabuvietv AB. Umaieg bsiepse apa Tesppoiodu 38, 413-420.

Filtration of effluents Biima S. M., Keeme 0. MU/., Nyzaip N., Kabiye N. E., apa

In the last 10 years, systems of final processing and membrane filtration have been developed. wastewater in the form of, for example, membrane plants - Mivmapaishap S, Mapd B-5., Mitsataga 5., apa novok (Viozsap A/5, Apzadeg Arz) and installations that MauiShtapikigamzh A. (1997) Arriisayop oi aig Brask use steam compression ( Rypki A/5, ViogpkKiaeg Pyvpipd ip tetbgape Biogeeasiog. U/aieg bsiepse apa

Mavzkiptargikkeg A/5). Gross processing cost of Thesppoiod 36, 259-266. 1m3 of manure by these systems is 50-100 dats- 7arts VA., Sogop-Watvigt A.-B. (Zepg A. (1996) kikh crowns. In addition, these installations are unable to convert other types of manure except pig liquid asiimaiea vipdde ayegayop o iapk.o Epmigoptepiai manure. Thesppoiodu 17, 1007-1014.

The reduction of the volume obtained by these installations is often no more than 50-6095, Thermal and chemical hydrolysis at a temperature that is, the scope of application of residues in any case below 100" C and, accordingly, a pressure of about 1 atm depends on conventional devices. That is, it represents one choice for increasing the availability of these plants are uncompetitive due to organic matter for biogas production. However, the level of costs and/or limited ability to reduce carbohydrates, for example, cellulose, hemi- sate volume. cellulose and lignin at such temperatures is hydrolyzed

However, it is important to think about and consider the level of not being completely caused. Fibers from straw, corn waste of these plants. It is also important to take into account that other crops are not used for the generation of electricity, caused by the mechanical compression of methane using such methods (Bjer- steam compression, i.e. about 50 kWh per ton re et al., 1996; Schmidt and Thomsen, 1998; Thomsen and processed liquid manure. This means that the mem- Schmidt, 1999; Sirohi and Rai, 1998). Alkaline-lime brane, considering that the water intended for filter evaporation at a moderate temperature above boiling contains only salts and a minimum number of and scale or sediment may be more advantageous than other (1997; Chanita et al. 1997; Chanita et al. 1998) evaporation technologies.

Reference: cellulose fibers from sugar cane, crushed

Agdatap U. (1984) bBipdie will enter pygodep noi into particles of size 0.5 mm (from 495 Sas, 2007" S and hetoma! ip ap ohidayop aysn. U/ageg Nezeagsi 18, 16 bar), splits cellulose into small organic 1493-1500. acids such as formic, acetic, lactic acid

Viotsip M., Vizayop .. skh., Vetsaeei V., apa Izpadye ti, etc. The output of methane from processed cellulose is

M. (1988). Vioiodisa! M/aziev 25,127-139. carbohydrates such as pure glucose (Azzam and Nasser,

Voshipariia E.N., Ait A.V., apa Viii55op N. 1993). Boilers can process (1998) Pishayop oi asiimayei viidde ivipo also green crops, but at a lower tempera- zyrtegdea tetbgape my aig ryrbiipo (arriisayop turi. According to published data of optimal yuyu zhmaziemagceg igeaytepi). Ophthalmology 118, 315-322. the result was achieved when acting on water hya-

Vypop S. N., Zpeai K. M/., Mizzeirgook T. N., cints at pH 11 and 1217 C (Patel et al., 1993). apa Raip V. B. (1998) docta! oh Adhisshshkai! The formation of RAS and substances that inhibit the action of

Epadipeegipud Nezeagsi 71, 203. ality of methane bacteria can be ensured

Satato I, Oia7 U. M. apa VKotego RE. (1996) at elevated temperatures (Varhegyi et al.,

Turnip! (eaytepiv og apaegorisapu aideviei riddegu 1993; Patel et al., 1993). However, this phenomenon is not uncommon. Viotavs apa Vioepegdu 11,483-489. Yuouie was observed at relatively moderate temperatures

M. apa de Ia Moce 9. (1987) Aegobis geaytepi oi rakh used in lime steaming vmipe tapige: Rpuziso-spetisa! regions Vioiodisa! compared to pyrolysis (Azzam et al., 1993). During

Maviev 22, 187-208. pyrolysis temperature is so high that biomass

Epadeinagaye M., Rik M/., apa M/atkep U/ (1998) decomposes immediately into such gases as hydrogen, methane

Ipiedgayop oi tetbgape Pgayop ip (pe asiimasei and carbon monoxide, and at the same time, unfortunately, and on RAS and viypide rgosevv ip tipisira! maviemaceg igeatepi. other pollutants of the environment.

Maieg bZsiepse apa Tesppoiodu 38, 429-436. Link:

Satamzhau 9. иЙ. (1982).

Sippimap M. 9. (1983) Tne eyesi oi ayegayop op apa Biodav Teppepiayop. wow! oh Epmigoptepiai! odoig apa zoiid5 oi rod vishpiev. Adhisishtga! Uaviev Zsiepse apa Epdipeegipd 28, 1629-1649. 7,197-207. Viegte A. V., Oiezep A. V., Rgetsivy T., Riodeg A.,

Sopeps Y.E. apa Naipetoev R. (1985) Zeptii: A. 5. (1996) Rgeigieaitepi oi mpeai v5igam/

ivipd sotbripei mei ohidayop apa aiKaiiipe Nuagoiuvov fields. M is also lost as a result of burning geziyipd ip sopmepirie seiPshShoze apa PpetisePPShozev. biomass

Viotesppoiodu apa Vioepdipeegipo 49, 568-577. Link:

Snapod M. 5., Majapi M., Noiiharrie M. T. (1998) Vesk 9. Sogeppepiaiop oi Iidtsii tapige apa reeiv az

Oedipus! apisiev - I Ite rgeigieaitepi oi shor gezidtsev5 a gedepegaime epegadu. Opimegeiu oi Nopepneyit, Oer. radazze apa uleai vigam. Arriiea Viospetivgu apa Adhiscishgai Epadipeegipd apa Apitai!

Vioyesppordu Rai A - Eplute Epdipeegipd apa Rhodysiyop. Reggzopa! sottipisayop

Viotesppoiodu 74,135-160. Spupomzhesh 0. R., Omepv .). M., apa Igedgapa V.

Spapod M. 5., Vagu V., Neugarrie M. T. (1997) Site (2001) Vepezhavrie temShape iot apaeegobis aideviyop rge-igeaitepi oi 5myspdgazz5. Arriei Viospetivighu og riotazz. Nepezhabrie Epegadu 22, 1-8. apa Vioyespppoiodu Rai A - Epgute Epdipeegpd apa Sypavzeeiap M. M. (1997) Apaegobis aideviopo oi

Viotesppoiodu 63-65, 3-20. Biotav5 Tog teipape rgodisiyop: A hemiem. Viotavv5

Sigheii M., Radda M. V., Kezsidpo A., Kipaiadi A. s, apa Vioepegadu 13, 83-114. Zodydy S., ZoiYai E., Massagdiy 5., Zapitsvi E., Vipaiiai Siviamuv5op I, Vogiezzop R., Vepadi 9., 5ueppipd55op

A. (1997). Rgosevv Viospetivighu 32, 665-670. Biotavz5 g go5v5ii Shei5. Epegdu 20, 1097-1113.

Heaven! M., Oeezai M., apa Madatuag 0. (1993) Tpegto Uezhmei! MU. 9U., bittipd5 V. 9., apa Visnagaz V.K.

BriotheiPapaiiop. Arriiei Viospetivighu apa Tahitit sopmegsiop Kipeisv apa ip 5yshi bBioda5

Viotesppoiodu 42, 67-74. rigiysayop Viotavkhz apa Vioepegadu 5, 261-278.

Zeptiai A. 5. apa Tpotzep A. V. (1998) Oriitizainop Uagmiz A., Mogaregd A., Uagizmik T., Maipiezep V., apa

OG mei ohidayop rge-meaitepi oi mpeai v5igam. Zmepz5zop V. N. (1997) Itrhometepi oyi a dgaz5-siomeg

Viogezoshgse Thesppoiodu 64,139-152. ziade-tey Biodaz rgose55 Bu She adayop oi soraiyi.

Zigopi 5, K. apa Nai 5. M. (1998) Oriitivayop oi Viotaz5 apa Vioepegdu 12, 453-460. Yeatepi sopayopv5 oi mpeai zigam/ my IPte: Ebesi Kysy R. ., Stov5m/pie MU. M. (1998) Tne adgisishshga! og sopsepigayop, toiizishge sopiepi apa igeagtepi (te gedshayugtu iatemzhok apa Bbiotav5 rhodisiop. op spetisa! sotrozyop apa ip mio aideviriyu. Viotaz5 apa Vioyepegdu 14, 333-339.

Apitai! Rhei 5siepse apa Tesppoiodu 74, 57-62. Ragvbru M. Nat 09 epegdiaggodeg - apaiuzeg ai

Tpotv5ep A. V. apa bsptias A. 5. (1999) Rypeg oKkopoti, epegdu od tio. Narrogi Mu. 87, bias(epv5 demeiortepi oi spetisai! apa Bioiodisa! rgosevzev g ChSchogarhydz od RizkepyoKopotivKe Ipziitsie. rgodisiop o oi bio eiShapo!: oriiytizayop oi rge- Zitve VA. N.E. (2001) Vioepegdu - a gepezharye sagbop ieatepi rgosizezegiv rgodisiv. vepk. Nepem"abie Epegodu 22, 31-37.

Visa Maiiopai I arogayushyugu, Rozkiide, Oeptaik. UMutap S B. apa Soodtap V. 9. (1993)

Magedui village, 57aro R., Mok UM. 5. And, Apa Apa)! M. 9. Viotesppoiodu og rhodisiyop oi ishei5 spetisai!5 apa (1993) Kipeis5 oi She Shepta! desotrozyop oi taiepaiv iPyot bBiotav5. Arriiei Viospetivmgu apa sebe ip zeaied mezvei5 ag eiiemayey rgezzihev. Viotesppoiodu 39, 41-59.

Washtai oi Apa|uiisa! apa Arriiea Rugoiuviv 26, 159- Vapk5 S 9. apa Nytrngeeuz R. M. (1998) That 174. apaegobris igeaitepi oi a Idpo-seiIshShiovis v!IBrvigaie

Silage of energy-intensive crops oMepypu She pashga! рН рыегипд сарасю. U/aiseg

Usual use of energy-intensive crops Zsiepse apa Tesppoiodu 38, 29-35: mainly in the form of solid fuel for spa- SopMegap E., UMiKie A., Wagu M., Gapepu o., S'"keiPu M. livation (shredded willow, straw or the whole zer- apa Aeupoidz R. 9). (1983) Ope apa eat ziade no) or as fuel for engines (rapeseed oil). Na apaegobis iYAKeg aideviop oi adzhisiishnta! maviev. Tniga experimental base beet and straw use- Ipi. Butr op Apaegobis Oideviop, 285-312, were cultivated for ethanol production (Parsby; Sims, Wozyup MA (1983). 2001; Gustavson et al., 1995; Wyman and Goodman, Oidba RM, apa 2napad V. (1999 ) Tgeagtepi oi Daigu 1993; Kuch 1998). In other countries, the practice of using energy-intensive crops has spread, many studies are being carried out - (peptoriie megziv tevzoriye. A properly documented oregayiopv. Viogezotsgse Tesppoiodu . the use of land, as well as sea and So5p 5., Otrgedi 9. R., apa Rirup R. (1985) of freshwater plants (Gunaselan, 1997; Jewel and Meipape rgodisiop iliyot ipaivipya! mavyez Bu imomo- others, 1993; Jarvis et al., 1997). Some dosli-rpase aidesiyop. U/a(eg Nezeagsi 19,1083-1088. The findings suggest that anaerobic U., Zcpdu 5., apa YuOadye V.V. (1997) Tetragaishge- fermentation of energy-rich cultures is con- rpasea apaegobis aideviyop curency to other types of biomass application (Chioi uaziematseg vishide5. MMaieg Zsiepse apa novetdD. P., Owens J. M. and Legrand R. 2001). Thesppoiodu 36, 367-374.

The use of energy-intensive crops has a good motivation. The use of straw is organized by Made! MA (1997). dippd (She apaeegobis (geaitepi tic promising for the coming years. Useful roshigu tapige. Uoigpa! oi Spetisa! Tesppoiodu tanya chopped wood seems profitable from apa Viotesppoiodu 70, 99-105. economic and practical points of view. On the other hand, Napsep K N., Apadeiidaki I., Ayipd V.K. (1998) burning of cereals caused resistance from Apaegobis aideviop oi 5mipe tapige: ipribyop Bu ethical considerations. Cereal production attopia. U/ageg VNeseagsi 32, 5-12. also inevitable is associated with the use of mineral fertilizers and pesticides and the loss of M on Apaegobis aidesiop rgosezz ipadeg maghisiv attopia sopsepigayopv.

Vioyesppoiodo 59, 349-352. plasterer A number of aspects, among others, are not described

Muapd O., Modispi S. K., Kypiporby M., Kaga U.H., such as pre-treatment, for example: alkali-

KaKitoyo K., Odamzha N. and I., apa Ka U. (1997) Hydrolysis, keeping animals on the farm, using

IpPyepse oi Puagashis gebepiop te op apaegobis tannia of energy-intensive plants, absorption of ammonia in aidezip o oi rge-neavy v5ishdde. Viostesppoiod in sulfur solution, precipitation of P, prevention of formation

Tesppidiez 11,105-108. struvite formation, etc. and the use of biogas instead of

Systems for disposal of animal corpses, etc. by gas engines or pipelines,

Current animal carcass disposal systems are designed for natural gas. apply to registered factories that have licenses for processing animal carcasses. is released from fermented organic fertilizer.

Animal carcasses are primarily used for A number of aspects are not described, among others, such as the preparation of meat and bone meal, which tradi- pretreatment, for example: alkaline hydro- used as livestock feed. liz, keeping animals on the farm, use

The current problems with cattle spongy - energy-intensive plants, the absorption of ammonia in the solution led to this practice with the implementation of the Sulfur Regulation, precipitation of P, prevention of formation

EEC, according to which meat and bone meal cannot cause struvite, etc. and the use of biogas to feed local livestock. gas engines or pipelines, pre-

Thus, before animal husbandry and related for natural gas. In these sectors of Europe, the problem has arisen as ЕРО286115 describes a method of obtaining biogas, in finding an alternative to the use of meat and bone-to which fatty cat meal is added to organic fertilizer or alternative ways of utilization of this lot or compounds containing fatty acids. Not torment. However, this is a difficult task due to limitations, a number of aspects are described, among others, such as encephalitis caused by the risk of the spread of prions - pre-treatment, for example: alkaline hydrolysis, noi sponge of cattle or other prions, it is possible to keep animals on the farm, use of energy substances in meat or other parts of animal carcasses. houseplants, absorption of ammonia in sulfur solution,

The use of meat and bone meal or sedimentation of P, prevention of the formation of struvite and half of animals by typical biogas plants, etc. and the use of biogas by local gas companies is naturally not recommended and is only possible with time-engines or pipelines provided by tkovo. Processing of animal carcasses by plants producing natural gas. have a license for the processing of such animals, usually EROZ351922 describes the method and installation, when it is carried out at a temperature of about 130 "С, with the separation of ammonia, carbon dioxide and phosphates at a pressure of about 2-3 bar for 20 minutes. Such is carried out from liquid organic fertilizer, Manure conditions at typical biogas plants are absent.is delivered from the farm to the plant by tankers where

The following patents and patent applications include hot air treatment and are related to the prior art. trace of this loses part of ammonia and dioxide

REZ 3737747 describes the installation and method of extracting carbon. The remainder of the liquid manure is heated, M. Sao adds to the manure, from which lime is released to a pH of 10-11, when bi-ammonia is released, this ammonia is adsorbed in an aqueous solution, less ammonia and calcium phosphate is formed. Extract containing hydrochloric acid. A number of aspects are not described that ammonia is absorbed in an acid solution, among others such as pre-treatment with the formation of an ammonium salt, which is dried and quenched, for example: alkaline hydrolysis, the retention is treated as a mineral fertilizer. For departments on the farm, utilization of energy-intensive crops, removal of solid particles from liquid manure, absorption of ammonia in a sulfur solution, precipitation of P, a decanting centrifuge is used. It does not describe the prevention of struvite formation, etc., and the application of a number of aspects, among others, such as pre-treatment of biogas with local gas engines or doing, for example: alkaline hydrolysis, retention by pipelines provided for natural animals on the farm, utilization of energy-intensive crops , gas absorption of ammonia in a sulfur solution, precipitation of P,

ОЕ4201166 describes a method of simultaneous processing to prevent the formation of struvite, etc. and the application of various organic wastes, in which the biogas separation waste by local gas engines or is poured into three fractions containing different amounts through pipelines provided for natural solid particles. Solid particles in front of fermen- gas. tation and release of biogas are homogenized. No. Е52100123 describes a method and an installation for cleaning - a number of aspects are described, among others, such as the cleaning of liquid manure. Organic components are pre-treated, for example: alkaline hydro-cleaved, precipitated solid particles are removed, keeping animals on the farm, disposal are energized using a decanting centrifuge. Acid is added to home cultures, absorption of ammonia in a sulfur solution, liquid and it is spilled on the precipitation of P, preventing the formation of struvite and poly, or it is further purified by aeration and separation, etc. and the use of biogas by local ammonia gas producers. The purified liquid is supplied to the water purifier by engines or pipelines provided by the shaft installation. A number of aspects for natural gas are not described. among others such as pretreatment, na-

РЕ4444032 describes the installation and the method in which, for example: alkaline hydrolysis, the keeping of animals on liquid manure in the first reactor is stirred, a-farm, the use of energy-intensive plants, is absorbed and lime is added to it to pH 9.5 for the reduction of ammonia in a sulfur solution, the precipitation of P , before ammonia release. In the second reactor, struvite-forming materials, etc., are added. and the use of salts containing iron and polymer for the purpose of natural biogas by local gas engines or pipelines

wires intended for natural gas. treatment, for example: alkaline hydrolysis, maintained

EK2576741 describes the method of obtaining biogasification of animals on the farm, utilization of energy-intensive pellets by fermentation of liquid manure. Liquid manure tour, absorption of ammonia in a sulfur solution, precipitation of P, treated with lime, precipitated prevention of struvite formation, etc. are removed. and application components. A number of aspects are not described, including the production of biogas by local gas engines or others such as pre-treatment, for example: pipelines provided for natural alkaline hydrolysis, keeping animals on the farm, and gas. lization of energy-intensive crops, absorption of ammonia in 5 4,329.428 describes equipment for anaerobic sulfur solution, precipitation of P, prevention of organic splitting, in particular, material from various struvite rennies, etc. and the use of biogas from local green plants and the use of extracted biogas. by gas engines or pipelines, the principle of operation of the equipment is a schedule that is in line with those provided for natural gas. is formed by mesophilic or thermophilic anae-

OV 2013170 describes the equipment and the method of dispersing bacteria. A number of aspects of biogas production are not described. In the first reactor, organic re- among others such as pre-treatment, manure is acidified and the solid frac- example: alkaline hydrolysis, keeping animals on tion is removed. The liquid fraction is fed to the second reactor, the farm, the utilization of energy-intensive crops, absorption, where anaerobic decomposition of ammonia occurs in a sulfur solution, precipitation of P, and methane is produced. A number of aspects, the formation of struvite, etc., are not described. and the use of biogas among others such as pre-treatment, on-site gas engines or pipelines - example: alkaline hydrolysis, keeping animals in dams intended for natural gas. farm, utilization of energy-intensive crops, absorption Оу54.579.654 describes the installation and method of ammonia in a sulfur solution, deposition of P, prevention of biogas production from organic materials. Solid ma- the formation of struvite, etc. and the use of biogas, the materials are hydrolyzed, acidified and fermented by local gas engines or pipelined. It does not describe a number of aspects, including those provided for natural gas. such as pre-treatment, for example: alkali-

RE19644613 describes a method of obtaining solid hydrolysis, keeping animals on a farm, utilization of mineral fertilizers from organic fertilizers (liquid sion of energy-intensive crops, absorption of ammonia in manure). A substrate is added to the liquid manure to extract sulfur, deposit P, prevent the formation of biogas along with CaO or Ca(OH)". Isolated struvite, etc. and the use of biogas by local ammonia is collected. It does not describe a number of aspects, such as gas engines or pipelines, before others, such as pretreatment, intended for natural gas. clade: alkaline hydrolysis, animal husbandry, 5 4,668,250 describes a method in which ammonia utilization of energy-intensive crops, ammonia absorption is removed from the liquid fraction by aeration. in a solution of sulfur, precipitation of P, prevention of the formation of a number of aspects, among others such as the formation of struvite, etc., are not described. and the application of biogas place- pre-treatment, for example: alkaline hydro-gas engines or pipelines, lysis, keeping animals on the farm, utilization of energy provided for natural gas. of domestic crops, absorption of ammonia in a sulfur solution,

РЕ19828889 describes co-fermentation of precipitation of P, prevention of struvite formation and poor harvest of crops and organic wastes from waste, etc. and the use of biogas by local gas producers. The material is homogenized and fermented by engines or pipelines provided. A number of aspects are not described, including for natural gas. others such as pre-treatment, for example: 5 4,750,454 describes an installation for anaerobic alkaline hydrolysis, keeping animals on a farm, duck decomposition of animal manure (manure) and utilization of energy-intensive crops, absorption of ammonia in cheap biogas, which was produced by with the help of sulfur solution, precipitation of P, prevention of the formation of this process. The principle of operation of the installation is the decomposition, destruction of struvite, etc. and the use of biogas locally, which is caused by mesophilic or thermophilic gas engines or pipelines, by anaerobic bacteria and uses mis- provided for natural gas. liquefied gas engines, 4,041,182 describes a method of obtaining feeds equipped with generators. A series of aspe- for livestock from organic waste is not described. It does not describe kts, among others such as pretreatment, a number of aspects, among others such as pretreatment, for example: alkaline hydrolysis, animal husbandry, for example: alkaline hydrolysis, farm maintenance, utilization of energy-intensive crops, absorption of animals on the farm, utilization of energy-intensive cultures, ammonia in a sulfur solution, precipitation of P, prevention of absorption of ammonia in a sulfur solution, precipitation of P, formation of struvite, etc. and the use of biogas to prevent the formation of struvite, etc. and application by local gas engines or biogas piping by local gas engines or dams provided for natural gas. pipelines provided for natural 5 5.071.559 describes the method of processing organic gas. ganic fertilizer. Water is added to the manure, this 5 4,100.023 describes the method and installation for the mixture is acidified. The liquid is removed to produce methane gas and mineral fertilizers. Aerobic decomposition takes place in the steam that condenses again in the other first reactor and undergoes anaerobic treatment to release the homogenized material. In the second area, there is biogas. Fermented liquid is a fraction that is heated, undergoes anaerobic digestion, which is then processed by an aerobic process. splitting and release of biogas. Mineral dob- A number of aspects are not described, among others, such as rivas are made in the form of liquids. It does not describe pre-treatment, for example: alkaline hydro- a number of aspects, among others such as pre-lysis, keeping animals on the farm, utilization of energy

domestic crops, absorption of ammonia in a sulfur solution, in the production of mineral fertilizers. CO" and / or Sabo" is added to the liquid precipitation of P, preventing the formation of struvite and manure with the help of etc. and the use of biogas by local gas plants, which emit ammonia. Not described by engines or pipelines provided for a number of aspects of the invention, among others, such as for natural gas. pretreatment, for example: alkaline hydrolysis, 5,296,147 describes a method of organic treatment - keeping animals on a farm, utilization of energy-intensive fertilizer (manure) and organic components. Organic crops, absorption of ammonia in a sulfur solution, wasp waste is fermented, and then nitriding of P, prevention of struvite formation, etc. and are fixed and then denitrified. /- Non-use of biogas by local gas engines - a number of aspects are described, among others such as ponds or pipelines provided for pretreatment, for example: alkaline hydrolysis, of natural gas. keeping animals on the farm, utilization of energy-containing 5 5.656.059 describes the method of processing organic crops, absorption of ammonia in a solution of sulfur, organic fertilizer, in which nitrogen is used as P, prevention of struvite formation, etc. and in the production of mineral fertilizers more or less use of biogas by local gas engines-nitrification. It does not describe a number of aspects of the invention or pipelines provided for, among others, such as pretreatment of natural gas. for example: alkaline hydrolysis, keeping animals on 5 5.389.258 describes the method of obtaining biogas for farms, utilization of energy-intensive crops, absorption from solid and semi-solid organic waste. Not ammonia in a solution of sulfur, the precipitation of P, prevention is described a number of aspects, among others, such as the formation of struvite, etc. and the use of biogas pre-treatment, for example: alkaline hydro- by local gas engines or pipe-laying, keeping animals on the farm, utilization by ener- provided for natural gas. home crops, absorption of ammonia in a sulfur solution, 5 5.670.047 describes the general process of anae-deposition of P, prevention of struvite formation and active decomposition of organic substrates, etc. and the use of biogas by local gas companies. engines or pipelines provided for 05 5.681.481 05 5.783.073 apa 05 5.851.404 for natural gas. describes a method and installation for stabilizing liquid manure. Lime is added to рН » 12 and the mass of heated manure, including a decrease in concentration, is heated to at least 50 degrees Celsius of nitrogen. A number of aspects are not described, including the 12-hour draft. Ammonia is released, and either such as pre-treatment, for example: lye- is released into the atmosphere, or it is recirculated hydrolysis, keeping animals on the farm, disposal- back into the system. It can be used for "chamberation of energy-intensive cultures, absorption of ammonia in preheating" as well as decanting of sulfur, precipitation of P, prevention of centrifuge formation, as well as mixing of sediment for utristruvite, etc. and the use of biogas by local residents in its liquid state. Sediment is introduced into the soil of the field by gas engines or pipelines. A number of aspects of the invention seen for natural gas are not described. among others, such as pre-treatment, on- 5 5.525.229 describes the general process and example: alkaline hydrolysis, keeping animals on the active decomposition of organic substrates in a thermal farm, utilization of energy-intensive crops, absorption of philic and also mesophilic conditions. ammonia in a sulfur solution, precipitation of P, warning 5 5.593.590 describes the method of separation and formation of struvite, etc. and application of biogasification of liquid and solid organic waste after local gas engines or pipeline separation of two fractions. The liquid fraction is fermented by natural gas. 5 5.746.919 describes a method in which organic precipitated solid particles, which are partially recycled, are treated in a thermophilic anaerobically in the process. The solid fraction passes through a reactor, after which it is treated in an aerobic process and processed in a mesophilic anaerobic reactor. In both reactors, methane is produced from compost, mineral fertilizers or feed for fattening animals. I wouldn't describe it. Part of the extracted biogas containing methane and a number of aspects of the invention, among others, such as

CO", pre-treatment is used again to reduce the level, for example: alkaline hydro-pH in the liquid fraction by absorption of CO". Solid particles are lysis, keeping animals on the farm, utilization of energy are precipitated from liquid fractions, for example, in home cultures, absorption of ammonia in a sulfur solution, using a decanting centrifuge, and ammonia is extracted by precipitation of P, prevention of struvite formation and is removed from the liquid using pH 9-10. Sewage, etc. and the use of biogas by local gas water can be used for cleaning engines or pipelines provided for the premises where the animals are. Not description - for natural gas. there are a number of aspects of the invention, among others, such as OZ 5.773.526 describes a method in which liquid and two pre-treatment, for example: alkaline hydro- organic waste is first fermented during lysis, keeping animals on a farm, utilization of energy using a mesophilic process , and after that, under home cultures, absorption of ammonia in a sulfur solution using a thermophilic process. Solid composition - deposition of P, prevention of struvite formation, and the dove part is hydrolyzed and acidified. Not etc. and the use of biogas by local gas companies describes a number of aspects of the invention, among others, engines or pipelines provided for such as pre-treatment, for example: alkali- for natural gas. 5 5.616.163 describes the method of processing energy-intensive crops, absorption of ammonia in a liquid fertilizer in which nitrogen is used as sulfur, precipitation of P, prevention of struvite formation, etc. and use of biogas by local farms, utilization of energy-intensive crops, absorption by gas engines or pipelines, pre-ammonia in sulfur solution, deposition of P, prevention seen for natural gas. formation of struvite, etc. and biogas applications 05 5,782.950 describes the fermentation of bio-local gas engines or pipeline waste with homogenization, aeration and dams provided for natural gas. mass heating. Waste is separated into liquid and UO8400038 describes the production of biogas and solid fraction. Carbonated and stabilized mineral fertilizers are made from the solid part. compost. The liquid fraction is fermented anaerobically. Thermophilic decomposition takes place in an internal mesophilic and thermophilic process with a reactor, and mesophilic decomposition in the release of biogas. Wastewater is fed from the biogas to the external reactor. A number of aspects of the so-called homogenization reactor are not described. Wastewater according to the invention, among others, such as pre-treatment of the biogas reactor is treated in a treatment plant, for example: alkaline hydrolysis, retention of water treatment. It does not describe a number of aspects of wine - animals on the farm, utilization of energy-intensive crops, running, among others, such as pre-processed - absorption of ammonia in a sulfur solution, precipitation of P, nia, for example: alkaline hydrolysis, keeping animals, prevention of struvite formation, etc. and applied on the farm, utilization of energy-intensive crops, absorption of biogas by local gas engines or ammonia in a sulfur solution, deposition of P, through pipelines provided for the natural process of struvite formation, etc. and gas application. biogas by local gas engines or pipe- УО8900548 describes the method of disposal of Са ions by wires provided for natural gas. and Mod ions in biogas production. Metal ions ha- 5.853.450 describes the method of obtaining pastel- foam formation. It does not describe a number of asperized compost from organic waste and zetas of the invention, among others, such as pre-washed plants. The pH of organic matter is raised to 12 and heating, for example: alkaline hydrolysis, keeping it to a temperature above 55 degrees Celsius. With animals on the farm, the utilization of energy-intensive crops, the addition of green plant material, the pH decreases - the absorption of ammonia in the sulfur solution, the deposition of P, is reduced to 7-9.5. The mixture is fermented. I will not describe - prevention of formation of struvite, etc. and a number of aspects of the invention will be applied, among others, such as the production of biogas by local gas engines or pre-treatment, for example: alkaline hydro- pipelines provided for natural leaching, keeping animals on the farm, using gas. energy-intensive crops, absorption of ammonia in a solution UM09102582 describes the equipment and method of desulphurization, precipitation of P, prevention of gas formation, and the method of preventing emissions in nakostruvite, etc. and the use of biogas by local residents to remove its environmentally polluting compounds in gas engines or pipelines, gas pre-washing. A number of aspects invented for natural gas are not described. course, among others, such as pre-treated 5 5.863.434 describes a method of stabilizing the soil, for example: alkaline hydrolysis, keeping animals ganic waste by splitting with help on the farm, utilization of energy-intensive crops, abso- anaerobic psychrophilic process. Not describing the sorption of ammonia in a sulfur solution, the precipitation of P, a number of aspects of the invention are supported, among others, such as the formation of struvite, etc. and the application of pre-treatment, for example: alkaline hydro-biogas by local gas engines or tubelysis, keeping animals on the farm, utilization by energy pipelines provided for natural gas. home cultures, absorption of ammonia in a sulfur solution, UM09942423 describes a method and equipment for precipitation of P, prevention of struvite formation and production of biogas. Fibers and particles from organic, etc. and the use of biogas by local gas fertilizers are composted, the liquid fraction is fermented anaerobically by engines or pipelines, and nitrogen is released. Ri K salts for natural gas. are used for mineral fertilizers by 5 6.071.418 describes the method and system of reverse osmosis treatment. It does not describe a series of ozone treatment of organic fertilizer with such methods of the invention, among others, such as a preliminary volume that forms aerobic and anaerobic processing zones, for example: alkaline hydrolysis, retention of melon material. It does not describe a number of aspects of farm animals, utilization of energy-intensive crops, the invention, among others, such as pre-treatment- absorption of ammonia in a sulfur solution, deposition of P, lation, for example: alkaline hydrolysis, retention of prevention of struvite formation, etc. and application - animals on the farm, utilization of energy-intensive crops, biogas production by local gas engines or absorption of ammonia in a sulfur solution, precipitation of P, pipelines provided for the natural prevention of struvite formation, etc. and gas application. generation of biogas by local gas engines or mlum.idr.to.de/UOmrio/"ep/Mapige.ep.peti describes pipelines provided for the natural method of obtaining biogas from organic fertilizer. gas. The solid fraction from degassed organic fertilizer- 1156,171.499 describes the improved method is used for the preparation of compost. From the fermentation of household and industrial waste, nitrogen is taken from the liquid fraction and used as

Waste is anaerobically hydrolyzed with the release of fertilizer. A decanting centrifuge can be used in combination with natural gas to separate solid particles from sub-biogas, which is used in gas turbines. Fermented ha. A number of aspects of the invention are not described. A number of aspects of the invention are not described, alkaline hydrolysis, keeping animals on a farm, waste, among others, such as pre-treatment, analysis of energy-intensive crops, ammonia absorption, for example: alkaline hydrolysis, keeping animals on a sulfur solution, deposition of P, prevention of formation

struvite formation, etc. and the use of biogas in the place of processing of animal carcasses, meat and bone by gas engines or pipelines, flour, etc. with animal organic fertilizers / intended for natural gas. by energy-intensive plant crops, proproper//pPega.seevia.ritadez/cryo tazv.pit nuating, thus, the method of disposal of corpses tva- describes the production of biogas through anaerobic digestion, etc., at the same time contributing to the production of decomposition. This system can use decanting of mineral fertilizers, which are made from an animal-killing centrifuge. It does not describe a number of aspects of their waste together with plant crops, organic matter, among others, such as pre-treatment with organic fertilizers, etc. lation, for example: alkaline hydrolysis, keeping The process makes it possible to use single animals on the farm, utilization of energy-intensive crops, annual fodder crops such as: beets, corn- absorption of ammonia in a sulfur solution, precipitation of P, dza or clover, all crops with greater prevention of struvite formation, etc. and application of dry matter per hectare than in grain crops. biogas production by local gas engines or Forage crops are also beneficial as "green cultiva- pipelines provided for natural ry" for crop rotation. This scheme has a demonstra- gas. watts energy potential when using ml. rioda5.sp/pye/tetep.pit describes the possibilities of lands intended for cultivation of energy content of reducing the content of solid particles in the mixture. such cultures.

The main and obvious idea - with all the variety of fixed film, ultrafiltration and circumstances - is that the production of biogas is reverse osmosis. A number of aspects are not described. In the future, this scheme will become competitive, among others, such as the previous processable, compared to natural gas, and it will be economical, for example: alkaline hydrolysis, keeping animals economically profitable, and mostly not will require the farm, utilization of energy-intensive crops, absotations. The idea also consists in the fact that the production of ammonia in a sulfur solution, precipitation of P, transfer of energy will make up a significant part of the consumption of struvite formation, etc. and energy use in Denmark, i.e. its order will be equal to biogas by local gas engines or pipe- order to use natural gas (about the wires provided for natural gas. 150 RU annually). In addition, the benefit lies in the odmmlu.rioda5.sp(ine/dgazravzi. pit describes the nature of environmental pollution, improvement of three-phase decomposition of ensiled energy-intensive manna of animals on farms and the safety of food crops and organic fertilizers, in which extraction of biogas. Two methods are described: 1. Silage- According to estimates of Parsbi's energy potential, energy-intensive plants are crushed for a period of time - when using energy-intensive crops, in particular, plasters of 1-3 cm in size and fed to liquid grain crops, annually will amount to 50-80 R). fraction containing organic fertilizer. A mixture of fer- At the beginning, it will require an area of 150,000 hectares, it is fermented at a temperature of 3570. 2. Dry fer- and in the future, 300,000 hectares. However, based on the fertilization of organic fertilizer and ensiled energy (yield) of dry matter in 15 t/ha of beets of domestic plants without adding another liquid. A number of aspects of the invention are described, not including the bottom, which will be processed, among others, in biogas production plants, the energy potential of such as pre-treatment, for example: alkali- will be about 100 R. annually. In addition to this, hydrolysis, keeping animals on the farm, utilization of energy from processed organic energy-intensive crops, absorption of ammonia in fertilizers (about 25 RU) will be added. New cultivars of beetroot sulfur, deposition of P, prevention of formation give the output of dry matter can be significantly over-extruded, etc. and the use of biogas by local shields today's levels, i.e. output of the order by gas engines or pipelines, pre- 25 t/ha. seen for natural gas. The essence of the invention lies in the combination of processes, etc. rioda5.sp/ne/251ede.pit describes the obtained, which allow increasing the production of biogas, ny biogas. Organic waste is hydrolyzed and sub-extraction of ammonia and its further use are acidified in a rotating screen-drum from which it is desired, and the processing of fermented, and the liquid fraction is sent to anaerobically treated residues (wastewater). vaccination, while biogas is released. It is characteristic that the essence of the invention allows combining a number of aspects of the invention, among others, simple and reliable technologies such as pre-treatment, for example: alkaline processes. It becomes possible to create a simple and rolyz, keeping animals on the farm, utilization of unreliable plant for energy production from prekras-rich crops, absorption of ammonia in solution by gray energy and economic indicators of ki, deposition of P, prevention of formation compared to conventional plants. Manufacturing plant, etc. and the use of biogas by local energy producers will further be integrated with gas engines or pipelines, pre-livestock farms and agricultural farms for natural gas. gifts Thus, the invention contains

This invention aims to demonstrate a number of aspects. a new way of using energy-intensive crops. The first important aspect is that this inven- namely: through anaerobic processing of tvan- the invention can be used for the purpose of combating in- manure from farms in production plants by biofections and the spread of animal microbial, and gas This process also includes the separation of rare parasitic pathogens, for example, campylobacter manure, that is, the extraction of nutrients from ter, salmonella, yersinia, ascaris and similar myco-animal manure. active and parasitic organisms, in the air and soil

This invention can also be used for land. The threat of human infection, thus

is reduced, or maybe completely eliminated. contains an extraction tank where ammonia is released

The second important aspect of the invention is the possibility of its use for the purpose of combating, for example, CaO and/or Ca(OH) by adding it to the extraction tank. However, adding Cao and/or Ca(OH)-containing prions of the encephalitic sponge of cattle to liquid manure can also be in organic fertilizer, fodder, slaughterhouse waste, and take place before feeding liquid manure to the first meat and bone meal and etc. This is achieved by a combination of pre-treatment or extractive pre-treatment and digestion. Like a tank. part of this aspect, this invention makes it possible At the same time to add Cao and/or to process animal carcasses, slaughterhouse waste, etc., Ca(on)", or at a later stage, the tank across- which makes possible the use of nutrient re - day processing, containing an extraction tank of iron contained in animal carcasses, as a mineral - performs the extraction process and/or heats them and fertilizers. Reduction of the amount and/or destruction of the produced nitrogen or ammonia must be absorbed prions of the bovine sponge contained in the carcasses of tva- before its storage in a separate tank (11). rin, meat and bone meal, etc., as well as in organically extracted nitrogen, including ammonia, should be absorbed in fertilizer, fodder, slaughterhouse waste, etc. while being in the column of the extraction tank that the process of the invention is a prerequisite for this is contained in the first tank of the previous person of waste processing. This is achieved according to the work before being submitted to a separate patent by a combination of pre-processing and processing for storage. cooking This technology constitutes an alternative Organic materials that are difficult to digest micro- today's technology (however, currently prohibited to roorganisms during anaerobic fermentation by the EC committee) processing animal carcasses in large, it is better to pre-process in the second tank of centralized plants and the manufacture of various pre-treatments (3) before submission to products, such as meat and bone meal, used in the first pre-treatment tank (2), which is mainly used as animal feed. contains the mining tank described above.

The third important aspect of the invention is that such organic materials usually contain a significant amount of its application for the separation of the main amounts, for example: cellulose and/or hemicellulose- nutrients nitrogen (M) and phosphorus (P) from cellulose and/or lignin, for example, more than 50905 (m//Lm) of ryna organic fertilizer and processing of feed-cellulose and/or hemicellulose and/or lignin on them into mineral fertilizers consuming dry weight of organic material, for example: salt-quality. we, plants, including corn waste, kul-

The fourth important aspect of the invention is the possibility of obtaining large volumes of biogas with heavy materials from motor plants and other solid organics. In the future, M is extracted from the pre-processed amount of organic substrates, including organic material, with all types of animal organic fertilizer, including ammonia. energy-intensive crops, plant residues and other organic waste in both the first and second tanks. after regular processing, liquid manure undergoes thermal processing

The fifth important aspect of the invention is lye or alkaline hydrolysis. However, the temperature and/or pressure to ensure optimal keeping of animals in the second tank is significantly higher than in the previous barns and to improve their living conditions by reducing dust and gas emissions, such as ammonia. a system capable of withstanding high pressure.

This is achieved by washing or recirculation. Finally, the liquid manure has passed through the previous drain through the cowshed. the aforementioned treatment, submitted to at least

The sixth important aspect of the invention is the possibility of a thermophilic reactor (6) and/or the possibility of benefiting from a number of advantages, less than one mesophilic reactor, which are due to various aspects of the invention. production of biogas (6). Liquid manure after this digestion

Other important aspects consist in combining anaerobically in reactors simultaneously from the essence of the invention with any one or more biogas production, i.e. gas consisting of these aspects. mainly from methane, which sometimes includes

Brief description of drawings of a small fraction of carbon dioxide. Bioga-

Fig. 1 reveals one of the important ways in which the challenge reactor(s) form part of the plant using this invention. This method of using energy for improved production consists in the fact that organic fertilizer, energy substrate of organic materials. preferably in the form of liquid manure accumulated in the Biogas can be fed to the gas engine, and the cowshed or room (1) for keeping animals - the energy produced by this engine can be used, including such domestic animals as dads to heat the production tank. However, pigs, cattle, horses, goats, sheep; and/or birds, for example, biogas can also be supplied to commercial biogas: chickens, turkeys, ducks, geese, etc., is placed in a pipeline that supplies domestic and one or two tanks of pre-processing industrial customers ki - the first tank of preliminary processing (2) Residues after anaerobic fermentation, all and/or the second tank of preliminary processing still in the form of liquid manure, which contains solid re- (3). metals and liquids, served, in this embodiment, on

The principle of operation is that the organic decanting centrifuge (7) for separating solid fertilizer, mainly in the form of liquid manure, including breath substances and liquids. One of the results of sepa- sion (in one embodiment) with water such as, for example, sewage, digging is a semi-solid fraction, which contains almost used for cleaning the cowshed, comes exclusively P (phosphorus), more than 50905 (m//Lm) P (12) . In the first pre-treatment tank, which is the same phase (7) or another phase of separation de-

tilting centrifuge (8), is also obtained described below. at least a semi-solid fraction that contains This invention contains a number of separate aspects, almost exclusively K (potassium), such as semi-solid which are described below. fraction containing more than 5095 (m/lm) K (13). These First aspect (sanitary) fractions, mainly in the form of granules, obtained The first aspect includes a system that consists- after the drying phase, including the phase that is drunk from the first component, a room for cooling drying or the drying phase of catching animals, including such domestic liquid manure, containing P and/or K with a purity acceptable for markets such as pigs and cattle, and/or the second consumer can be excellently used as a component, mainly for the separation of ammonia for commercial mineral fertilizers (10). and pretreatment of the substrate, and/or the third

Such mineral fertilizers can be used as a component, mainly of the plant for the cultivation of agricultural crops or in the fields. Fluids poured energy production from the substrate. (9), which also come from the separation phase of the deka- The system can consist mainly of a centrifuge, such as effluents, can also be fed to the agricultural land, they can be fed back to the tank and the biogas reactor. Additional components of livestock premises, or to water treatment parts may include a device for adding structures. to liquid manure CaO or Ca(OH)", absorption

Residues from anaerobic fermentation, still in a column operating on the basis of, for example, a salt form of liquid manure containing solids and acids, a storage tank for a concentrated liquid, in this embodiment are fed to an ammonia decanter and a storage tank for processing - centrifuges (7) for separating solid liquid manure. wines and liquids. Produced biogas can be used if desired

In a further embodiment, organic materials can be supplied to the first tank for the production of electric current of pre-treatment, or heat with a gas engine and generator, electric materials from the silage tank (4) containing river current are usually sold electrically compa- capable of fermenting organic materials. Submissions, and the heat is used for heating, heating such organic materials to the first re- for example, a room for animals, or heating a reservoir of pre-treatment may contain a phase, liquid manure. According to the invention, the production plant includes anaerobic fermentation, for example, the flow of energy has excellent productivity expressed in the reservoir of thermophilic fermentation, capable of producing energy per unit of substrate, transferring gases from the silo. In addition to the straw and the one made at the factory. This excellent productivity of agricultural crop wastes obtained from agricultural land (5) is achieved by a combination of pre-treatment can also be fed to premises for tri-processed substrate, organic animal manure, and then to the first and/or second fertilizer or of another organic substrate from the pre-treatment tank. removal of ammonia from the substrate before anaerobic digestion

Fig. 2 illustrates the embodiment mainly as a drawing. shown in Fig. 1, with the only difference that after the separation, the advantages of this invention are described in detail below. One of the main aspects is only phosphorus (P, water in the form of effluents is collected at the site - sanitation, which includes pre-treatment in a separate tank for further cleaning, - alone or in combination - a number of separate phases before - including further removal of nitrogen, destruction of the day of treatment , which are detailed below: odor and most residual solids). Pre-treatment of liquid manure after issuing

This can be done, for example, with the help of len from the room can include any one of anaerobic fermentation. Potassium (K) can also be separated from one or more of the following phases: 1) release (mining) of ammonia, 2) hydrolysis of organic matter, 3) sanitation

Fig. 3 illustrates an embodiment containing simplified container processing of liquid manure, 4) pinout reduction - approach to the system of combined separation of bio-fermentation, 5) flocculation, 6) precipitation of P, 7) gas and liquid manure in accordance with this invention - warning formation of struvite. move This embodiment does not use fe- The principle of operation is that the liquid manure rmenters of biogas, and the solid substances obtained in the comes from the first means to the extractive res- as a result of pre-treatment in the reservoirs of rvoir where ammonia is released due to the addition of pre-treatment one (2) and/or two (3) pro- CaO or Ca(oOnH)", it is released, heated and separated by a decanting centrifuge (4 is absorbed in the column before entering the and 5) after separating M including ammonia and collect- storage to the tank At the same time, liquid manure is stored in a separate tank (8). Thermal or alkaline hydrolysis, preferably separated and semi-solid fractions containing RIK are obtained using a processing lime aggregate. (9 apa 10). Finally, pre-treated liquid manure over-

Fig. 4 illustrates an embodiment where potassium (K) is not filtered to a third means consisting of a mono-evaporated after separation by a decanter or two thermophilic / mesophilic reactors by a centrifuge, as described in the embodiment according to biogas, where liquid manure anaerobically is processed

Fig. 3. However, it is possible to further separate K with the release of biogas, for example, the gas that consists of waste water and its collection. consists mainly of methane with minor

Figures 5 and 6 illustrate the implementation of the system in carbon dioxide solutions. Biogas is supplied according to the present invention. The individual components of the gas engine, the heat produced by this engine, are described here in detail. is used to heat the minable

Further embodiments of this invention in detail tank. The produced electric current pro-

given to electric companies. Accordingly, if there is a need to add

Since straw and, possibly, sawdust is an important tissue control of foam formation and/or part of the litter in the premises to maintain flocculation in the process due to a very large yield- livestock and birds, there is a need for a special hug of gas, then Ca and/or rapeseed oil the processing of these organic fertilizers is submitted before the optimal mo in the fermenter. Addition of Ca(OH)" or CaO using as substrates for production will also cause precipitation of such bicarbonates as methane in biogas plants. In this regard, SasSo." This will reduce the concentration of CO" in the solution. One of the best methods of pretreatment is in the gas phase and will contribute to the reduction of foaming. Lime digestion under pressure. Litter processed by the reduction of carbon dioxide emissions technology can be used this way. for the production of methane in a more efficient way and the addition of Ca(OH): or Cao in connection with the production of biogas. ammonia treatment and liquid sanitation

In addition, it is ensured that uric acid and manure will also cause the precipitation of orthophosphate, urea is decomposed into ammonia and that dissolves - for example, dissolved P (Roy). These P particles are proteins and other substances. This also ensures that other flakes can float in the liquid manure, collecting inorganic nitrogen from the litter in the form of a suspension. The use of Ca also contributes to the nitrogen concentrate by means of the extraction process, which will produce a limited reduction in the consumption of ammonia chemistry. of oxygen (SOI), which will mean that Ca precipitates

Therefore, the presence of M in pods will also increase significantly, and other salts, not only orthophosphate. rump and bird droppings for agricultural crops. It is believed that, regardless of the chemical difference, the potential efficiency of use between different products of organic waste can be increased to about 9095, which is actually heat treatment and, in particular, heat treatment in the form of other manure processed at the plant in combination with alkaline hydrolysis provides increased biogas production and separation of liquid manure in the production of gas. Moreover, the combination of compliance with the present invention. high temperatures and high pH during the pre-

On the other hand, it may be more convenient to process organic manure in the first ter- treatment of organic material compared to only a mo- or mesophilic reactor to its ultra-anaerobic digestion, thermophilic or to the extraction tank. It depends on mesophilic. depending on the quality of the fertilizer (manure) and to what extent the uric acid is regulated in Regulation Me823 of Denmark due to two different methods of processing. Clarity will be brought to this by accumulated energy. processing is 1 hour at a temperature of 707 C.3

It is important to note the versatility of the plant, considering that it is considered that processing according to makes it possible to process all types of manure and embodiments of the invention, which is one week of energy-intensive agricultural crops. processing at a temperature of 70" C before two

The technical design is relatively simple: a screw conveyor, equipped with a shredder, completes all (thermo- or mesophilic) made of stainless and acid-resistant steel, known veterinary and/or human microbial and zoono- feeds the biomass into the treatment tank. lime kills pathogens. The prions of the cattle sponge are also destroyed - the mass is heated by starting steam to 180-200"C. that all infectious organisms

The designed installation should be capable of organisms dying in liquid manure and therefore not spreading to create temperature and pressure in the temperature in the environment during the spreading mode of 100 - 2007 C. Based on this, fertilizers on the fields. It also makes it possible to easily adjust the processing into different types of the first means (premises for keeping animals) of the biomass processed at the plant according to the invention- processed liquid manure for the purpose of cleaning, taking into account the method of energy use, piggery, cowshed, etc. Thus, foam formation and technical parameters are prevented. there is cross-infection among animals. It

A general problem of biogas plants is the opportunity to use water for foam formation. A reliable method of control is the washing of animals and premises, air extractors and foaming at biogas plants, etc. without emissions of odors, dust, and infection into the air, when a large number of these microorganisms enters the plant. This is possible, because the liquid manure of biomass from, for example, energy-intensive agricultural crops, with additional water will not be stored in periods of rapeseed oil, which, in addition to the properties of control, allowed accelerated land use. foaming is also a substrate for M-free liquid manure can be applied to the field during the formation of methane gas. Sa ions, like many salts, all year round. is also a very effective means of combating the formation of However, in the first aspect, it is the previous precipitation. One of the best measures to control bka and, thus, sterilization of liquid manure to foam formation according to this invention is Ca(OnH)»2, which allows its further application on agricultural land. and baoO in addition to their other aforementioned It is clear that the present invention relates to a number of properties. It is believed that the addition of Ca ions to the genera- various aspects that make up, taken separately or in which manure stimulates the formation of flakes and in combination with others, a patented invention for their adhesion of bacteria to organic particles and, in its own right. The following section contains how anaerobic fermentation is achieved. description of various separate parts (components) of one aspect of the present invention. Overview of the components of the circulation system. One of them is placed under the cover in Fig. 5 and 6. with a coating up to 30-357"С, it provides pigs

It is clear that the selected components can create a pleasant microclimate, keep the floor dry and form the basis for other aspects of this inhibits the growth of bacteria on the floor. The second search system. This invention does not limit in any way - it supplies heat to the entire room through pipes, by combining (combining) the entire list laid along the walls of the pig house. The second system of components described below. It is clear from the description that it is connected to the ventilation control. lym when other aspects of the invention relate only to Souls: Souls are better arranged above the plates of some of the components described below. Not limited to frequent steps that cover 95% of the entire floor area, examples of such aspects include floor facilities. This forces the pigs to defecate on M (nitrogen) and/or P (phosphorus) concentrator steps rather than on a hard floor. Shower water and/or K (potassium); the resulting energy production will flush the manure down the drains, thus avoiding waste on the components of the extraction tank, lime-ammonia, odor, etc. A clean and hard floor of the digester tank and fermenter significantly reduces possible infections from pathogens in the litter, making water used in the premises, for example: salmonella, and ausopia etc.. for animals and sewage 4) Flushing: Drainage channels are flushed

It goes without saying that the following several times a day. This is ensured by the aspects related - among other things - to the washing of the channels with technical water from the production plant to the aspect of sanitation, must not necessarily contain energy. Organic fertilizer is applied to all the following components. Aspects of the central channel through the valve. are related to sanitation, must contain 5) Channel design: The surface of the scum of the combination of only some of the following is compensated due to the simultaneous use of nts. of M-shaped channels and optimal circulation

Livestock premises with canals. This is very important for reduction

Animal premises (component number 1) of emissions from premises where animals are kept. are designed to ensure optimal safety 6) Ventilation: Ventilation is arranged and quality of feed, optimal living (maintenance) in such a way that 2095 maximum ventilation- animals and working conditions for farm personnel, ventilation is carried out under the sabers and through them, until optimal harvesting of liquid manure, suitable central ventilation shaft, between double for processing at the power plant with organ- M-shaped channels. In 60-8095 per year, 2095 mechanical substances, and minimizing emissions in the ventilation simum is sufficient to ensure the environment (ammonia, dust, odors, lack of proper ventilation. methane, nitrous oxide and other gases). 7) Feeding: Feed is supplied by equipment

The room can consist of one or a kilo of feed, which provides the animals with as many piglet sections as they want, a total of 10 feeds. sections designed for growing 250 heads per Tank for collecting liquid manure. year. Each section is designed, for example, for 640 The tank for collecting liquid manure (compo-piglets (7-ZOkg) or 320 adult fattened nents number 2) is designed for collecting pig manure (30-98Kkg). after daily cleaning of the room for

The expected annual amount of production of animal manure and to be an intermediate reservoir of manure is about 10,000 m3. In addition to before it is pumped to the main collecting volume through the livestock room of the prole tank. Liquid manure is fed to the collector - 5-10,000m3 of technical water is collected. For the installation of a tank based on the principle of gravity. The following main conditions must be created: a suitable volume is taken, somewhere around 50 tons. 1) Two-climate system: Pig pens must The tank can be built from concrete and placed be provided with a two-climate system. it is below the floor level of the room, such that

The rear end of the pigsty should be equipped so that liquid manure from the premises flows into the collecting tank through a suitable device (cover). the pigs have the option of choosing between the relatively warm Main reception tank under the cover and the relatively cold Liquid manure from the collection tank pumping- part of the rest of the pig house. The temperature difference to the main receiving tank should be 5-10 C (component number 3). Other types of liquid

When the piglets reach a weight of about Zbokg, manure/waste can also enter the receiving tank from farms/factories. Exceptions are the lower temperature prevailed in the pigsty. Pigs are kept warm under the manure of mink, v.r.h., molasses, bard, silage, etc., thanks to their feathers. Lowering the temperature makes it possible to improve the ventilation of the cargo and is unloaded directly into the receiving tank, also during the cold seasons. voir Volume / capacity is the value 2) Behavior: Pigs receive straw from auto-order about 1.000t3. The level in the mining mat-dealer. This stimulates searching and digging, the tanks can be controlled by a pump, which will pull the straw out of the machine themselves. pumps liquid manure from the receiving tank.

Straw also serves as a source of energy at the plant Dose adjustment can be both manual and automatic for energy production. parent The maximum power is set- 3) Heating: Heat from the production plant depending on the circumstances. energy in livestock premises is recirculated. Heat can be supplied by two separate When liquid manure is pumped from the receiving

of tank 1 to the extraction tank, lime is added to the System of supply and homogenization of sub-liquid manure to increase the pH. rearing and energy-intensive agricultural crops

The lime addition collector is adjusted to the power. The supply of lime (component number 8) for bedding and is energized in the form of a powder that can be blown into domestic agricultural crops received an energy-intensive tank from a truck. The volume/capacity of spare organic material from screw conveyors in the cellar can be, for example, 50-75 tons. Dose from the receiving station. Energy-intensive s/g crops 30-6OGh / kg T5 corresponds to approximately 6-12 kg Sas on can be supplied by additional augers with a capacity of 3.5 t / hour of liquid manure fans to digestion (processing) units and with 695 T5. be simultaneously crushed by the built-in shredder

When added directly to liquid manure, use The volume / capacity can be large (69o T5), the dose of lime is about god / kg T5, necessary for specific circumstances, for example (about 8.8 kg Sao per hour). However, it is better to deposit about 1.5 m3 of energy-intensive agricultural crops / add lime directly to the sterilizing unit, or 8,200 t of energy-intensive agricultural crops / year. lysis with lime under pressure and hydrolysis. When adding it is desirable that the power of the lime feed system directly to the device with pressure (energy-homogenization was at least about 30 home-intensive organic material E has 20-70 95 T5), m3 / hour. Three main parameters to control - the dose of lime will be approximately 30-6oOg / kg T5. the addition of energy-intensive agricultural crops, for example / kg of dry matter equals approximately 342 kg of yield, weight per volume, and time. With these parameters

Sao per batch, and ZO g /kg of dry matter, equal to the volume per unit of time will be set, approximately 171Kkd Sas per batch. and therefore the total volume and weight.

Setting the weight Pressure lye sterilization unit and hydro-

The scale (component number 5) will weigh the super-chololytic chewing E (energy-intensive organic material). The unit for sterilization with lye under pressure and hydro-

The suppliers will clarify the type of material that is lyzed (component number 9) serves two purposes, and can be supplied to the plant, for example, litter, me: firstly, to destroy pathogenic microorganisms - energy-intensive agricultural crops, etc. of different types. had in energy-intensive organic material,

The specification should be made by choosing, in particular, the litter from birds and other animals - the appropriate energy-intensive organic material of the Nitsky farms and, secondly: the simultaneous hydrolysis on the control panel. According to the registration of the panel of post-structural components of the bedding for the purpose of their sub-chambers, the weight of the obtained energy preparation for microbial decomposition in fermenters is registered. of energy-intensive organic material, including speci- The unit will also destroy or significantly reduce energy-intensive organic material. number of bovine spongiform prions, if they are present in the

Thus, the control bodies determine the processes that have arrived at the plant. Such waste contains, for each energy-intensive organic material, meat and bone meal, animal fats and the like (see alkaline hydrolysis): substances from the processing of animals not used for -Energy potential of consumption. -Time required for heating Filling of pressure sterilizer ensures

Litter reception station and energy-conformity to the type of energy-intensive organic material: material as determined when setting the weight.

Reception station (component number b) Digestion (processing) unit accepts litter from, for example, poultry farms or pressure consists of two identical blocks, and litter from other animals, as well as energy-intensive agriculture, namely: two elongated tubular horizon- cultures. It is desirable that this station be a large lin chamber with a central auger. These two pipes with a tank equipped with several screws are attached one above the other in order to facilitate the conveyors in the floor. Trucks unload and sew the loading of the lower pipe. The blocks are covered with their load of energy-intensive organic mate- with a hollow lid on the underside. This rial lid goes directly into the tank. The volume / power will direct heat to the energy-intensive material can be set depending on the steam under the lid. circumstances, for example, the annual capacity of energy-intensive Lime is added to the upper processing organic material (about 51,595 T5) of the block from the Sas tank, namely 342 kg for about 9,800 tons. The volume of the tank can be a batch. The lower pipe is preheated from a few cubic meters to about 100 muU, for that energy-intensive organic material from the upper three days of power (65 hours). The material is the desire of the block. but concrete / steel. The lower pipe empties into a small

Reservoir for energy-intensive agricultural crops, a shoaling tank containing 25 m3. Here energy

The tank for energy-intensive agricultural crops (compo-intensive organic material is mixed with liquid nent number 7) serves to ensure the storage of manure from the receiving tank 1, then the mixture of energy-intensive agricultural crops. Energy-intensive agricultural crops are pumped to the extraction tank. preferably canned as silage. Volume / capacity The CaO pipe contains a bypass, so the CaO can be, for example, about 5,000 - add directly to the mixing capacity of 10,000m3. The tank can be a closed box with two pipes under it. The mixing chamber is used, where the silage juice is collected and pumped to mix the sterilized energy (pumped) to the receiving tank. solid organic material and liquid manure from the receiving tank to obtain homogeneous - Energy potential for each energy-intensive biomass and re-use of the heat of energy-intensive organic material. - Time required for heating

The main processing parameters are - Time required for processing the content of dry matter in energy-intensive organic - Time required for mixing with liquid material, temperature, pressure and pH. With a large number of possible combinations, the optimal parame- - The use of the necessary energy depending on the tram settings are as follows: temperature 160 "C, pressure 6 bar from energy-intensive organic material, dry matter content about 3095 and pH close to - Degree of filling, signal from radar / microwave 12. microwave measuring device

Processing time in the sterilization unit - Quantities based on empirics consists of several phases: 1. Filling period; (practical experience) depending on the visual con- 2. Preheating period in the upper pipe; troll operator 3. Heating period in the lower pipe; 4. The period of pe- Mixing capacity for sterilized reprocessing of material at a given temperature and under pressure of energy-intensive organic material and pressure; 5. Period of pressure reduction; 6. The period of evaporation of liquid manure. harvesting and 7. SIR (washing) period. After sterilization and hydrolysis in a pressure re-

The filling phase consists of the time required for the processed biomass to feed the energy-intensive organic reservoir to the mixing tank (component of the material to the pressure sterilizer and its variable number 10), placed, preferably, under the pressure solution with added liquid manure. Halfway through the period. Excess pressure (steam) will be released for about 10 minutes. After being transported to the extraction tank for ammonia collection and filling, the energy-intensive organic material of the heat transfer to the extraction tank is bioheated to 160" C at a pressure of 6 bar. The mass before entering the mixing tank is heated in the upper pipe, and the heating in the lower pipe.

The period of material processing at the desired temperature of the tank with hot sterilized energy temperature and pressure will be about 40 minutes with a capacious organic material to ensure (at 160" C and a pressure of 6 bar). heat transfer (heat reuse).

The period of pressure reduction is approximately and mixing of both substances. minutes The pressure is released to the production reservoir. The volume / power can be on the reservoir. the deposit is about 25m3. You can use any

Emptying is ensured by turning on any suitable material, including insulated screw conveyors. fiberglass. The working temperature is usually

SIR period. Cleaning is carried out from time to time, in nov. 70-95760. in principle, there is no need for it. Reservoir for liquid biomass.

The volume of the pressure tank for digesting liquid biomass contained in the tank for (processing) is 10m3 per block, and the volume of liquid biomass (component number 11) used for digestion is approximately 75-9095. The volume of the mixture - ensuring the receipt of a sufficient amount of the bio-valve tank is 25m3. gas during the start-up phase of the entire plant. However, this

Below is an example of process conditions. may be used occasionally when such liquid biomass is available. Liquid biomass will include, for example, fish oil, and animal or 000000 dalazone given| one | vegetable fats. You can use both bard and molasses, but it is not very desirable due to the relatively 95% of the total water content and therefore the low content of potential 10-30 30 weight of total energy per 1 kg of product.

The volume / power is usually about 50 m3, the suitable material for the tank is stainless steel. The contents of the tank are mostly liquids and solids, size le) | in b particles of which is the maximum ZMM. A stirrer is installed, as well as a heating system for temperature control, the fermenter(s) are supplied with pump(s). The temperature should preferably be at least 75"C in order to be able to pump to the fermenter(s) the oily

On the panel of suppliers, where energy or fatty biomass is recorded. | | And domestic organic material, will be determined Gas extraction tank and sanitary ob- the following for controlling the sterilization unit: weight, work | | And the volume and type of energy-intensive organic material. To the gas production tank | sanitary

Thus, it is possible to determine for each treatment (component number 12) the following energy-intensive organic material that comes in! And to the pressure tank for digestion, - Liquid manure from the receiving tank 1 the following: and/or

- Energy-intensive organic material from the boiler. Volume / Power: The cylinder wall has an inner diameter of about 12m and a height of Wm. This is possible - Liquid biomass from a liquid tank has a working volume of about 1,000 m3 of biomass, and/or including a bottom cone. - Used technical water from the decanter. The period of hydraulic processing for liquid or possibly after separation of K. manure and energy-intensive substance is about 7

This tank is designed to regenerate days, and the absolute minimum treatment time for the heat used in the digester is approximately 1 hour. under pressure by heating liquid manure from the receiving Optimum embodiment: the bottom is made in a straight tank 1, for mixing energy-intensive concrete, reinforced iron and insulation, which is an organic material with liquid manure and thus withstands a certain pressure. The surface in contact with the nom, to obtain a homogenous mass for the enzyme material, is coated with isophthalic polyester teres, to adjust the pH before entering in order to avoid corrosive damage to the fermenters, and for sanitary treatment of liquid tone and reinforced iron. All are installed at the bottom of the manure. pipes are made of polyester or stainless steel

Mining tank and sanitary steel tank. The top and bottom are basically sealed processing releases ammonia, phase |, the gas enters the isophthalic polyester "sandwich" (sealed absorption column, which is typical for the final soap). All installed pipes are made of polyes- selection process, phase II. Pathogenic microorganisms, or stainless steel. washes are destroyed and the substance / liquid manure is ready for Other components: anaerobic digestion (processing). - The mixer is made of stainless steel

The following form may be offered - Heating elements are made of mild extraction tank and sanitary steel tank with coating and/or stainless steel finish: - All other components contained inside

Tank bottom/floor made of stainless steel. - With an insulated concrete cone, direct- In one of the optimal implementations, the values of it downwards at an angle of 20 degrees standard parameters for the release of ammonia from - The used mixture / sand is removed from the liquid manure in this system are: Temperature- logs or in accordance with large pumping system about 707 C; pH is about 10-12; the fate of the liquid topic of gas « 1:400, 1 week of work, is reached over - A sand filter is arranged at the bottom, which is 9095 efficiency. can be emptied through an externally connected tru- Below is an example of operating parameters: bu. There is also the possibility of emptying the reserves - Material: All types of liquid animal manure and slurry through a filter. sterilized under pressure

Top/ceiling solid or liquid energy-intensive material, different - Cone made of isolated isofatal- liquid organic waste, Sao. of polyester "sandwich" (sealed foam). The working temperature angle: 70-80" of the cone is about 10 degrees. The composition of the working gas: 8095 MNa, 1595 СО", 3905 02, - Mounted water spraying system 295 other gases to combat the formation of foam in the mixing process - Insulation parameter k: 0 ,20 MM/flow and in the process as a whole.Maximum working pressure: 420 mbar abs (Vacuum- - No mixing system is installed on top of the cone) slow-acting shearing to ensure optimi- Maximum density (viscosity) of the material: 15965 homogenization, optimal evaporation T5 (tensile strength) of ammonia and optimal distribution of heat in the alkaline/acid range: 5-10 рН rho-containing organic matter Abrasive particles in the material (sand): 1-29 - Ammonia enters through moist air through a pipe The maximum temperature in the heating elements of the absorbent unit is 90 degrees Celsius

Side / wall The maximum power in the heating elements - with a cylinder construction of insulated isophats: 600 kW tal polyesters "sandwich" (hermetic pi- Transmission force: 7.5 kW / 20-25 rpm per). From the mining-sanitary tank, the treated material is mounted inside the tank and enters the fermenter(s) on 600 meters of heating 5/4" pipes in the form of a cylinder. In the timed (timed) ra - rings for heating the substance; during the process, the material will flow to the fermenters. - Several temperature sensors are mounted for The need for material depends on the processes of readjustment of the heating process; cooking (processing) in the fermenters. The mounted device for measuring pH can be used one, two, three or bi- to regulate the flow of acid to the material of fermenters. Alu; Mining and sanitation tank regularly - On the outside of the cylinder wall, an iso- iso- is filled with liquid manure and an energy-intensive place for the valve/pump is mounted on the bottom; material from the alkali treatment process under pressure. On- - Ammonia vapor diffuser is placed in the middle of the remaining dry matter is extracted -1595 (159515). tank. Ammonia vapor produced in the unit Several level control switches regulate the alkaline sterilization and hydrolysis is sprayed into the ma- the contents of the tank. Device for measuring T5 material. adjusts the value of T5 (tensile strength).

Every hour after filling the liquid manure meters of heating pipes (5/4") in the ring-shaped and energy-intensive material, the energy-intensive material can be pumped to the fermenter reactors by a cylinder). - To regulate the heating process, the

The top of the mining-sanitary tank is ventilated, several temperature sensors are placed through the ammonia absorption unit (step ), and - To regulate the flow of acid to the device for measuring pH, it regulates the need for energy-intensive material is installed / pH-

Sao gauge

The temperature of the energy-intensive material is regulated by temperature sensors on the outside of the cylinder wall at the bottom (bottom). space for isolation valve/pump

The time-bound process can optionally The volume / capacity of each tank can pump water / liquid manure into the system spread any suitable net volume, including spraying to reduce foaming. net volume is about 1,700m3.

Fermenters for obtaining biogas. Materials for fermenters can be

Processing (digestion by bacteria) of the following materials: The bottom of the biomass is provided by a multiphase system - The bottom is made in principle from concrete, ar- fermenters, preferably from three fermenters (compo- matura and pressure-resistant insulation nents 13,14 and 15). Can also be used - The surface, which is in contact from the perero system with both less and more vomited matter, is covered with a layer of isophthalic fermenters. of polyester to avoid corrosion damage

Fermenters are connected to ensure maximum flexibility and optimum yield of concrete and reinforcement - All pipes installed at the bottom are made of polybiogas. Fermenters are planned for operation of ester or stainless steel at thermophilic (45-657C) and mesophilic Top and wall (25-457C) temperatures. - The top and walls are made mainly of soft

The processing process (digestion of steel by bacteria) can be optimized according to the speed of loading - All installed pipes are made of organic polyesthetization, material processing time and ru, stainless steel or mild steel of maximum digestibility (min. 9095 M5). Other components

Heating coils are included for heating the biomass - The mixer is made of mild steel to the desired operating temperature. - The heating elements are made of soft

A slow-acting mixing system with a closing steel top ensures optimal homogenization and heat distribution throughout the biomass. tank bowls made of stainless steel

The pH can be adjusted by adding organic or mild steel acid (liquid) in the required amount. Working conditions can be any

Fermenters receive the following substances: given conditions, including: - Energy-dense substances from mining - Energy-dense substance: all types of animal sanitary tank manure, primarily liquid manure from pigs. - Liquid biomass from the tank for liquid biomass - Shredded energy-intensive agricultural crops. Some discharges of organic waste, Sas, organic acids - Acids from the acid tank Operating temperature: 35-56 "С

The specific shape of the tank in the optimal embodiment can be: other gases

Bottom/floor Insulation value k: 0.25 M/tgK without heat rating - With insulated concrete cone, directed in 10 kW downwards at an angle of 20 degrees Maximum working pressure: 20 mbar abs. - The used mixture/sand is removed from the soil (no vacuum) using a powerful system of pumps. The maximum density of the recycled material is - A sand filter is installed at the bottom, its faults: 1295 T5 can be drained through an external pipe connection. Range of alkali/acid level: 5-10 pH

The tank can be emptied through the filter. Abrasive particles in the material (Sand only):

Top/ceiling 1-295 - Conical structure made of mild steel. Angle The maximum temperature of the heating element is approximately 10 degrees; ments: 80 degrees Celsius - Installed a water spraying system with Maximum power of heating elements to reduce the formation of foam during the process: 600 kW mixing and general process Transmission number: 7.5 kW / 20-25 rpm - Slow-acting mixing system ensure- Digestion (decomposition) is carried out at optimal homogenization and distribution of 55"C. Heat loss is estimated at approximately 10 heat from biomab. kW. Biomass in the tank can be heated from 5'C - Biogas enters through moist air in the pipe to 55" C for 14 days, it is possible to add acid to the gas tank. lot for pH regulation.

Side / wall Reservoir for organic acids for regulating - The cylinder is made of mild steel pH in Fermenters - For heating energy-intensive material There is also a tank for organic acids - about 600 acids (component number 16) are installed inside the tank for regulating pH in fermenters . From the bottom of the column, now ammonia-free water

The buffer tank for the degassed liquid is pumped to the outlet pump of the controlled level. manure in front of the decanter The separated ammonia enters the bottom of the two-stage

After digesting the biomass in the fermenters of the new gas washing column where the ammonia gas is used, the degassed biomass is pumped to a small cold condensate buffer tank (component number 17) that is condensed in the countercurrent of the ammonia. Uncondensed ammonia gas is further separated by separation in a decanter. condenses in the counterflow of pure water (perhaps

Decanting unit (component number 18) penetrate from the final stage of reverse osmosis). designed to remove suspended particles If there is a desire or need to use (55) and P from biomass. acid, then at this stage it is necessary to use sulfur

The decanting unit separates the digested biochar. In this way, it is possible to achieve a higher final mass by two fractions of the solid concentration of ammonia. substance, including P, and its) spent water The gas scrubbing column is made of poly- measure in order to make it possible to use

The fraction of solids contains 25-3595 dry acids. substances Approximately 9095 55. and 65 are extracted - Ammonia absorption column (to use 8095 P content in the digested biomass. In the case of the first and/or second extraction of M) addition of PAH (Firm "Ketiga Oaptagk") in the buffet - Gas scrubbing column (condensate scrubber) ry tank before separation in the decanter serves to ensure flexibility in relation to dora, it is possible to extract about 95-9995 R. Fraction of giving acid. The column (component number 21) of solids enters the tanks through the dopo- consists of two sections, therefore the fraction of ammonia, by means of a shaftless screw conveyor. that did not condense in the first section, in the further

Waste water contains 0 -195 55 and the solution is condensed in the second section. This occurring K. 55 depends on the addition of PAH. It is based in full countercurrent, so the addition of water as a component of the waste water is dissolved as much as possible. Thus, the K content, which is about 9095, is reached in the initial and final output condensate. Waste water is pumped with a high concentration of ammonia (more than 25905). It flows to the waste water tank. the liquid product can be pumped out with a separate pump

The system for transporting P-fractions and recycling or collecting through the valve on the circulation pump. Absorption can be promoted by adding sulphur-

From the decanter, the fraction of solids (the initial acid in the counterflow of water.. it is usually called the P-fraction) can enter the Sulfuric acid tank to a number of containers with the help of screw conveyors. acid, which is used in the formation of the P-fraction (component number 19). during the M selection process (component number 22).

A regular conveyor belt carries P- Reservoir M5 (nitrogen storage). fraction to the warehouse, where it is assembled and covered - Tank M5 (nitrogen storage) (the component is a compost cover, there it is transformed - number 23) is intended for storing the allocated compost. The process of composting further M. dries the P-fraction, the content of dry substances such Storage of gas. thus increases to 50-6095. It is desirable to provide for gas storage (compo-

The second phase of allocation M nent number 24) as a buffer storage for

It is desirable to obtain effective allocation of ammonia power, for example, to the electric motor of the generator. from waste water, and it is also desirable to get a tank for sewage (waste water). the final level is approximately 10 mg МНА-М / l or less waste water from the decanting unit. is pumped to the waste tank (used

It is desirable that the second phase of extracting water is carried out) (component number 25). The tank was cleaned by using a steam stripper for sewage (waste water) equipped with a (mining unit) that works with a proper immersed microfilter of static action. Pressure microfilter. The principle of operation of the stripper is based on the removal of particles larger than 0.01-1 mm. On the difference between the boiling temperatures of ammonia and water. Ammonia is secreted most effectively when a negative pressure of 0.2-0.6 is formed in the membrane. From here, the dissolved substance is absorbed at a temperature close to 1007 C. The use of energy cuts the membrane, and the particles remain on the surface for heating the working substance - this is an important function of the membrane. To avoid decay and the formation of a working parameter. Therefore, the stripper block after scale on the membrane, the sediment on the membrane should be thoroughly heated before its arrival with the help of periodic procedures to wash the stripper column to the temperature of approx. 100"С. This is ensured by the use of steam (or possibly hot water and steam) from the electric oven. It will automatically perform the extraction of the accelerator-generator in the steam-water heat exchanger. of the substance and the procedure of reverse circulation.

After heating, the working raw material enters the bath. Extraction will be interrupted by the stripper column and seeped over the column, with periodic backwashes, for example, simultaneously heating up to the operating temperature of the deposits: for 35 seconds for every 300 seconds of time by a counterflow of free steam. Steam/ammonia gas then con- jobs. The flow will be 2-6 mZ/hour. densed in a two-phase condenser (gas produc- To help with microfiltration, a washing column can be used). apply aeration. Aeration creates a sharp impact on the surface of the membrane, reducing scale and decay. steam production. This pair serves as a source of

Further, it aerates the waste water and stimulates the heating of the plant's processes, for example, in the unit, the aerobic decomposition of residual organic rechvirilization under pressure and in the p-striper I! (mining, nitrification and denitrification. Thus, reservoirs) (in the first place). Depending on the number of steam bones destroyed during the microfiltration process, it can also be used for residual odors, nitrates, etc. concentration of K in waste water (evaporation

Forging substance is dissolved from this tank). will be installed for: Between the steam and heat circuits, a heat exchanger is installed - Cleaning with water washing of livestock houses, so it is possible to transfer the heat of rooms, channels, steps, etc. heat from the steam system to the heating system. -Further separation. Dissolved K concen- In addition to the above-mentioned kit, a steam boiler is also installed. This K will be stored in a separate storage boiler and will serve to produce heat for the tank. Water for cleaning by washing the start of the process, in addition, it will serve as a support water for livestock premises can also be used for a set of equipment. take solute from this stream. If more steam is produced than needed, K can also be concentrated in other ways for plant processes, then the rest of it can be liquidized, for example: with the help of a mechanical or blowing in a refrigerator. steam compression (compression). It will depend on the specific selection of the fermenters for starting the plant process (heating the res.) etc. heat is supplied from the plant and the amount of excess heat, the existing boiler, which runs on fuel oil. Once started for vapor compression. receiving gas, this boiler will switch to gas

The used water tank containing the burner, as soon as the gas production reaches a volume sufficient to start the engine, as soon as the gas production reaches a concentrate from the microfiltration, this engine will run at regular intervals to take over the heat production. lation of concentrated particles. This add- Getting potassium. goes either to fraction K or P from the decanter. At least two alternatives are possible for

Reservoir for K (component number 26) for the release of potassium from waste water (the component is filled to store potassium concentrate (K). number 29). With relatively large amounts of

Gas purification and biogas are produced by an engine with a generator

Biogas produced by fermenters can replace excess heat (steam at 160°C), which can be used to extract trace amounts of hydrogen sulfide (НБББ5), which is used to concentrate K. Freed from must be removed (component number 27) before the nutrients of the distillate it can be used by burning biogas at a combined plant with vyvata for field irrigation or recirculation throughout the plant's heat and energy production.

The gas will be purified using the ability of certain aerobic bacteria to oxidize NO5 into biogas in relatively small quantities, a microfilter for sulfate can be used. First of all, it will be a bacterium filtering particles larger than

TNiorasiiy5, which is known for its distribution in several 0.01-0.1 ut from waste water, which directs terrestrial and marine environments. Bacteria such as Tpitisgozriga and a standard reverse osmosis filter can also trap a solution of material suitable for processing. To wish-

ZY OIoriv. but concentrate to a solution of 10-20965.

The tank is made of fiberglass, ob- The second aspect (cattle teeth prions). arranged by plastic pipes with a large In the second optimal aspect of this invention, the surface area that should be poured can be used to significantly reduce the ringed water to keep the material wet and/or destroy the prions of the bovine sponge, which Biogas is fed through a blocked column and contained in manure, fodder, slaughterhouse waste, meat- air flow (atmospheric air) is added to bone meal, etc. This is achieved by combining the biogas flow. Atmospheric air is added for pretreatment and digestion (processing - obtaining an oxygen concentration of 0.295 in the gas stream, fermentation) by microbes. This component, as mentioned, is sufficient for the oxidation of He and in order for it to be supplemented with a device for additional creation of an explosive mixture of biogas and oxygen. Pre-treatment of the substrate containing prions is carried out by a ring side blower. cattle sponges, for example, a pressure boiler with vapor

Combined plant for the production of heat and nom. Processing with the help of lime can use energy (SNR). be used for the hydrolysis of a number of organic substances

The main component of SNR (a component of norats, including materials containing prions. mer 28) can be, for example, a motor that works Prions of cattle sponges are proteins resistant to gas action, this motor is connected to a generator for protease. However, when processing with lime from the temperature - production of electric current. The main fuel is preferably 140-180"С, the pressure is preferably 4-8 bar, and the function of the SNR is to produce as much electricity as possible. At a pH of about 10-12, prions are partially hydrolyzed and, energy compared to heat. This engine is preferably begin to be decomposed by the water circuit (907 C), and heat by microbial enzymes, such as proteases, amidases, etc. Microbes are present in bioreactors and the like, for example, rooms for keeping tva - that ammonia is removed from the substrate and there is less total M compared to total carbon

The spent gas is used in the recuperator for this, microorganisms are able to produce additional extracellular proteinases and proteases capable of hydrolysis in the decanter. call prions of bovine sponge. A long period of time They can be used in the fields of processing will also contribute to the effective, based on the specific need in each nutritional cleavage of spongiform cattle prions. substance There is also the possibility of recirculation

The third aspect (concentration of M and R). (reuse) of waste water,

In the third optimal aspect, this invention, taken outside the decanting centrifuge, can be used in the room to separate the main animals. Nutrients of nitrogen (M) and phosphorus (P) are added here from cleaning the floor and manure and processing (refining) these gradually in cowsheds, and this is an additional advantage from nutrients to mineral fertilizers for the consumer, given the good climate of the cowshed. reduction of koi or "organic" quality. This is achieved by emissions of ammonia and other gases, frequent washing by combining the components of the first aspect from the runoff channels of liquid manure, etc. centrifugation with a decanter. Waste water may contain the main

M and P are the main nutrients in the liquid fraction of potassium (K), and a smaller part of the potassium (K) fraction, which is often in excess in the premises for umthium, is in the fraction of P. This means that in a situation where animals are ruminating. M is released and collected as ammonia is extracted from liquid manure and it is separated, described in the first aspect, leaving P in remaining for the separation of P, M and P can also be stored in processed liquid manure. However, if used according to specific needs, centrifugation takes place in the decanter P, while the waste water can be used from liquid manure along with organic manure and not be used as sewage throughout the year. ganic solids. According to estimates, the need for space for distribution

As a result, more than 9095 M and P of liquid manure will provide about 95 of the area required for the wound in separate fractions. Residual spent liquid manure application, harmonizing area and water contains a certain amount of potassium (K) and trace rings, 1/4 part will pass through the entire harmonizing M and R. Thus, spent water healing area during a 4-year period . see for use in the fields at any time Regardless of the possibility, I will continue to process the year. wash (purify) waste water (see development

It is possible to extract potassium (K) from the waste water) some farmers will undoubtedly be more than water by means of additional simultaneous membrane satisfied with the extraction of M and P by only one rea- aeration and filtration. In short, ceramic ktorom for processing liquid manure. It is even possible to use microfilters simultaneously as diffusers and filters. Filters are immersed in waste water, because M concentrates leaving a diluted bath water and are used in periods of aeration and liquid manure without M, which can also be applied in alternating filtrations. Aeration provides nt in the fields at any time of the year, with the exception of the breakdown of residual organic matter and frozen soil. deposition of inorganic flakes. Thus, it is very good that farmers can be offered, treated water is suitable for membrane parts of the entire system, while other filtration, because rotting and scale are avoided. They will also be satisfied with any combinations, more and aeration through the same membranes (washing with water- necessary for their needs. In any case with oral air flow) protects the membranes from the very extraction of M causes the interest of farmers to rot and scale. before using a decanting centrifuge.

The resulting product is a concentrate (which, depending on the requirements of the market, the used water is mainly K) and filtered water, suitable for the entire process can undergo final treatment for use in the field (required a very limited area). Thus, the task is to

As in the first aspect, the waste water can also be recirculated around the premises to obtain water suitable for membrane- keeping animals. filtering and also greater reductions in volume

Fraction P is suitable for further drying than the mentioned 50-6095. In addition, the task of watering, which gives a granulate acceptable for consumption, is also to use the well-known, chiv. Fractions M and K are also suitable for commercial cheap and reliable technologies in a new context. sales The following solution is proposed:

The third aspect is, in particular, a scheme for the concentration of the main nutrients M and P (K) in liquid manure. . substrates for the production of mineral fertilizers Aeration achieves the following: for commercial sales. First, residual ammonia is released and

However, if the decanting centrifuge combines - is collected in an absorption column (perhaps with other elements of the CEE separation system itself, which was used during the pre-biogas and liquid manure, in particular with the unit for its processing) using the so-called low-extraction M, it causes considerable co-temperature release at about 207 C interest among farmers. The combination of extraction of M and decanting- The necessary wider liquid-gas ratio, of the blast centrifuge means that most of the content of Mi R zko 1-.2000 (Paoega!. 1995). in manure, it is separated and collected into separate fractions. Secondly: the residual organic fraction is decomposed. It is important to note that P, if it is present in the substance and the smell is destroyed (Satagego ei ai. 1996; flakes, doomed to release a centrifuge- Vypop ei a! 1998; YuOouie apa MoPe 1987; Sagamzhau

1982; Sippimap 1983; Viotsip yes!. 1988). In addition, the processing system in CEE biogas

Thirdly: possible ammonia residues after extraction and separation ensures re-application will be nitrified to nitrate (Agaatap U. nia of nutrients in the fields. Energy-intensive plants 1984; Sopeps apa Nagtetoez 1985). lines are digested in a separate reactor and

This aeration will be combined with filtration - the processed biomass is fed to the extraction tank using new tank processing technologies. In this tank, fibers that are not sewage waste, for example, according to the principle of micro-recycled during their stay in a separate refiltration combining aeration and filtration-reactor, are hydrolyzed, and ammonia will accumulate in them through ceramic filters (Voshpariia ei ai. 1998; fractions M. Azot M , which is contained in energy-intensive soybean plants, can then be recycled to 1998). Energy-efficient aeration and filter fields and used in the cultivation of new tubs are achieved in one operation. In addition, energy-intensive agricultural crops. Can be re-aeration used for cleaning ceramic used about 1-3kg M per ton of silage. membranes by the method of "reverse purification of air" (Mizmapatyanp ei a! 1997; 5iima ei a! 2000). but to process to release ammonia from it, which,

This makes the aqueous phase well adapted, particularly at thermophilic temperatures, inhibits separation through standard osmotic mem- biogas process (Napzep ei ai. 1998; Kguyuma ei ai. branes if necessary, because they are reduced to mini- 1997; Kaupapiap 1994). Ammonia is released during pre-treatment of the sludge, where the biomass is also hydrolyzed - scale and rot problems are possible. Therefore, it is accepted, etc. it is assumed that it is possible to achieve a larger volume. It is desirable to divide this process into thermophilic reduction with much lower energy consumption, and mesophilic components (Yuydra apa 27papd despite the consumption of a certain amount of energy 1999; Nap ei ai. 1997; So5P ei a). 1985; SoPegap ey for aeration. AI. 1983). This makes it possible to increase production

Even if no membrane fining of energy and stability of operation is used, among other filtrations, the separation in itself justifies the reasons and because the biomass remains longer in the final release of ammonia and elimination in the reactors, which gives the methane bacteria time for the residual odor. cleavage of the substrate. It should be noted that for

The fourth aspect (renewable energy). heating requires a larger amount of energy

The main means of the optimal aspect are only a larger total volume of the reactor. pre-treatment units consisting of In addition to this two-phase principle behind the extraction tank and the water treatment unit will use another reactor for lime, and a flexible and multi-phase (at least From the pre-digestion of bird droppings and phase) process scheme of bioreactors. similar biomasses with M content. In this rector and

A fourth optimal aspect of the invention can be used to obtain large volumes of digestible energy-rich crops before further processing at an energy plant. Pro-biogas from a significant amount of organic substances, during the first digestion, the main fraction, including all types of animal manure, energy-organic material that can be easily purchased - high-energy agricultural crops, crop residues, etc., is split, and nitrogen is released into the solution in other organic waste. in the form of ammonia. Now the nitrogen can be separated into

Aggregates for pre-cleaning the first and former tanks and collect them in fraction M. of the second optimal aspects of the invention make it possible to use a number of organic substrates, etc. contain about kg of M per 1 ton of wet weight, therefore, and the multiphase biogas plant makes it possible for this M to accumulate in the M fraction of complete digestion (processing) in a way, to get the maximum same to be processed in the pre-treatment before the production of energy. subsequent digestion (processing) on

Rich in M and heavy substrates, for example, pta- main biogas plant. tire dung and litter are preprocessed- Separation and hydrolysis provide what is melted in the lime treatment unit. Before the skin and heavy fibers are subjected to digestion, the arrival of the lime-treated substrate to as described for preliminary processing. After the extraction tank and further reactors, it is digested at the main biogas plant and is pre-processed (digested) in order to ensure maximum gas release. mesophilic reactor. The fifth aspect (life of animals).

Preliminary processing (digestible) ensures decomposition and release of nitrogen to be used to provide an optimal solution in the form of ammonia of organic matter, which is easy to acquire. In this way, the mass of nitrogen M accumulates while simultaneously reducing the emission of dust and fumes in the extraction tank, and heavy organic gases such as ammonia. This is achieved by washing the night substances are decomposed in the following reactors or by recirculation of waste water according to plant examples. Alternatively, depending on the quality of the puppy for the purpose of cleaning and washing the boxes, floor, substrate, it can go directly to the steps, channels for the removal of manure, etc. . As a result, large volumes of odor, ammonia and dust can be released. we use biogas, for example, usually 5-10 times more. In addition, the system enables the use of co-energy than was contained in liquid manure. scraps without increasing dust and ammonia emissions. Solo-

Ma is an important component of the life of animals, substances and liquids that come, for example, or from in particular for pigs, as well as for other animals. pre-treatment of organic material

It gives them the opportunity to burrow in it and provides and/or the release of M, including the release of ammonia, for them to occupy and structural feed. and/or anaerobic fermentation causing

The production of biogas is well suited for washing animal boxes. At the same time, it is possible to reduce the waste water taken after de-treatment and/"or to destroy the appearance in the waste water by a tilting centrifuge (third aspect) or, possibly, microorganisms by further purification steps. ly, after the first digestion (the first aspect. ). Washing removes straw and pus from the mixture of cheap mineral fertilizers as a commercial admixture from steps (stands). by clear standards. This is achieved by separating

In further optimal aspects, any combination of the main P-containing granulates and K-containing granulates of the invention with other mentioned aspects is preferred, including the release of ammonia and separation. By pre-decanting centrifugation after the previous aspect, it is desirable to include it in all combinations. its treatment, preferably including thermal

Accordingly, from the previous descriptions it is clear what alkaline hydrolysis is. aspects and embodiments of the present invention, which are contained in In another aspect of the present invention, it is proposed to give preference to: a method of reducing the number of living microbes and/or

The method of improved production of biogas, prions of the sponge cattle, present in organic material, and the above-mentioned method consists of the following materials, and the above-mentioned method consists of stages: from the following steps: i) allocation of M, including ammonia, from organic materials, its acquisition of organic material that is mixed materials including ordinary and liquid manure, as well as solid and/or liquid particles; the desire to hydrolyze organic material, i) i) reduction in the above-mentioned organic

By feeding the thus obtained organic material of the amount of live microbes and/or prions to the biogas fermenter, and) obtaining a sponge of cattle, by feeding this organic material to biogas by fermentation of organic material. to:

The above-mentioned method may, in addition, contain a) Phases of treatment with lime under pressure, and/or a phase of separation of solids obtained from p) Phases where the organic material is heated by biogas fermentation in the phase of separation from a predetermined temperature and/or is subjected to the action of - using a decanting centrifuge. From this charged pressure and/or added alkali or separation, separate fractions P and/or K, acid, and/or, preferably in granular form, are obtained. c) Phases where at least partial occurs

The above-mentioned method in another embodiment can hydrolyze organic material, have a further phase of recirculation of liquids, and the above-mentioned phases of processing a), B) and them from biogas fermentation according to livestock c) can take place indoors, if desired, after the cleaning phase. simultaneously or sequentially in any way

In another optimal embodiment, step M is included in the line, and in connection with the extraction of ammonia, it is desirable to obtain processed organic material simultaneously with, or sequentially after, any material containing at least a reduced amount of the order, using the thermal guide step - live microorganisms and/or prions of cattle sponge. rolization and/or the step of alkaline hydrolysis, where the method of the invention makes it possible to destroy one or both of these steps at an elevated temperature of a number of microorganisms, including micro-organisms and/or elevated pressure as described by animals belonging to microorganisms , above infectious microorganisms and parasitic pathogens

Thus, the above-mentioned optimal embodiment of micro-organisms, including any of them in one embodiment, solve problems, connection. These include, but are not limited to, undesirable micro-organisms caused by environmental pollution, such as campylobacter, salmonella, ganisms, including Zaitopea Turpitigicht, yersinia, roundworms, and similar microbes and parasites.

OT104, and/or prions, sponge-related microorganisms, as well as viruses, viroids, etc.

HCVs present in organic materials, including ordinary and liquid animal manure. serves for sterilization of organic material, c

In another embodiment, the aforementioned optimal phase destroys all living microorganisms. Vap-incarnations solve the problems associated with the provision of a sufficiently high standard of hygiene in baking with CaO or Ca(on)". cowshed or piggery. This is achieved by reducing any VUOE prions or other prions present in the destruction and/or destruction of unwanted micro-organic material is destroyed or removed by the sterilization process. When there is a reduction in the present in organic materials, including zvi- microorganisms and/or prions after any of the tea and liquid animal manure. of the above steps, then it will be reduced to

In yet another embodiment, the aforementioned optimal e.g. 9095, reduction by 8095, reduction of the embodiment solves problems associated with excessive 7095, reduction by 6095, or reduction on it using expensive water in livestock premises preferably at least 5095. This problem is solved repeatedly. In one embodiment, it is desirable to improve the extracted use of waste water, the production of biogas by processing organic material from the separation phase with a decanting centrifuge under pressure before being fed to the furnace used to separate solid fractions of M However, organic material treated with lime under pressure can also be fermented.

If the organic material has plant growth, a reservoir for its storage. After being absorbed into the gin, it is desirable to ensilage the separated nitrogen M, including ammonia from the nitrogen, before feeding it to the separation column. It is acidified in a column containing water or an acidic digested organic material of the plant compost, preferably sulfuric acid, before it can also be fermented until separation by extraction and reaches a storage tank. from it nitrogen M. Organic material for silage- In one optimal embodiment, it is provided that the fodder cultivation method consisting of such phases as beets, corn, clover, and where desired) removal, inactivation and/or a decrease in the above-mentioned organic material of the tops (tops) of plants

Treatment of organic material with lime under live microorganisms and/or prions of the sponge of cattle, under pressure, preferably takes place at a temperature of supplying organic material to: about 1007 - 2502C, under a pressure of 2-20 bar, with up to- a) Phases of treatment with lime under pressure, and/or , giving lime sufficient to obtain a level of p) Phases where the organic material is heated to pH 9-12, the processing time will be from at least at a given temperature and/or it is acted upon by a predetermined 1 minute to preferably less than 60 minutes. pressure and/or alkali or acid is added to it

The amount of added lime, including CAO, and/or preferably from 2 to about 80g per kg of dry matter c) Phases where at least a partial substance occurs, for example from about 5 to about 80g of hydrolysis of organic material, where the aforementioned per kg of dry matter substances, for example from about 5 to the processing phase a), B) and c) can be carried out about bOg per kg of dry matter, for example from simultaneously or sequentially in any order, about 10 to about 80g per kg of dry matter, i) selection M including ammonia from the above- for example from about 15 to about 80g per kg of dried processed organic material, dry matter, for example from about 20 to about iii) directing organic material of which 80g per kg of dry matter, for example from about 40 released nitrogen, to the biogas fermenter, up to about 80g per kg of dry matter, for example from them) fermentation of organic material, from about 50 to about 80g per kg of dry matter, from which nitrogen was released, for example from about 60 up to about 80 g per kg sum) to obtain biogas and fermented organic matter. material with a reduced number of live ones

An example of the operating conditions of the microorganism and/or prion processing unit is cattle sponge. lime can be temperature in the range from It is very important that in organic material from about 120"C to about 220"C, pressure from about 2 bar to preferably less than 18 bar after fermentation, and the time of operation . from at least 1 minute to preferably less than In the nitrogen release phase (M), including ammonia, minutes. it is desirable that it take place first in addition

Another example of workers can be tempering to organic material amount of lime, gilding in the range from about 1807С to about statin to increase the pH level to about 9 20"С, pressure from about 10 bar to preferably less at a temperature better than 40" C, for example, than 16 bar, the pH level is from about 10 to about 12, the pH level is above 10 at a temperature and the working time is from about 5 minutes to about 10 better than 40"C, then, for example, the pH level is more than 11 at a temperature better than 40"C,

The above-mentioned method can be supplemented, for example, the pH level is above 12 at the temperature of additional phases. In one embodiment, the pre-temperature is better above 40"C. Further phases of feeding the processed organic material to the biogas fermenter are desirable in optimal embodiments, but to be above 50"C, it was, for example, during the fermentation of the processed organic material, above 55"C, for example, over 60"C. and production of biogas. Another further phase of sto- In one embodiment, the working time is from 2 to 15 days, for example from 4 to 10 days, for example from alu to the external environment, including s/g 6 to 8 days. An example of a set of parameters: the pH level of the land. Application of processed organic matter from 8 to 12, temperature from 7070-807C, proportion of material to the external environment, including agricultural land, liquid to gas is less than 1:400, the time of work by fleas can also be carried out by using every 7 days . Alkaline conditions can be provided by the residual material obtained from fermen- by applying any alkali. However, the pH is better for the growth of processed organic material. to protect by introducing Sas or Sa(on)".

Another further phase is the release of nitrogen (M). Organic material can contain solids, including ammonia, from the above-mentioned organic and/or liquid particles, for example, ordinary and liquid material before the application of organic matter - animal fertilizers, residues of agricultural crops, silage to biogas fermenter. This ensures crop waste, animal carcasses or their parts, wastes and stabilization of biogas production. This slaughterhouse, meat and bone meal, including with any of them, will also make it possible to use nitrogen-rich combinations. In one embodiment, the organic mater-

M of biomass for its selection and subsequently for al contains a maximum of 5095 solid particles, after digestion in fermenters. Biogas production - an example of a maximum of 4095 solid particles; is produced as a result of the fermentation of organic matter with a maximum of 3095 solid particles, for example, material from which at least a maximum of 2095 solid particles was isolated. Organic matter - part M, including ammonia. the material can also be in a liquid state and contain a maximum of 1095 solid particles. it is waste water received from a plant for the production of

The organic material may include straw, biogas production, or waste water obtained during the concentration of phosphorus fertilizers, or the material has a high fiber content, preferably waste water obtained during the concentration of more than 1095 (m /m). Organic material can also be potash fertilizers or collected rainwater. have a high content of complex carbohydrates, which mis- It is desirable that any or most of the networks of cellulose, and/or hemicellulose and/or lignin, iron and/or uric acid contained in the or- for example, more than 1095 (m/ Li). Treatment with organic material was converted to ammonia, where some material containing cellulose with lime under ammonia is optionally collected after absorption under pressure, causing the cellulose to split on the non-column, as described elsewhere. large organic acids, such as formic, acetic, Additional phases in addition to the processing of lime, lactic and similar acids. nom under pressure is mesophilic and/or thermophilic

Organic material may also contain sub-fermentation. Accordingly, organic material, tailings or animal manure, in particular from cattle, pigs, which has been treated with lime under pressure, and birds. In addition, you can use tva- further sent to the plant for mesophilic organic material, for example, corpses and/"or thermophilic fermentation before or after animals or their parts, slaughterhouse waste, meat- release of nitrogen from organic material. bone meal, blood plasma or similar substances. Each fermentation is carried out by a strain of bacteria of animal origin, risky and non-risky, which are able to provide appropriately heated material, given the presence of prions, a philic or mesophilic reaction. Fermentation in sponges of cattle or other prions. In one embodiment, this is anaerobic fermentation .

In one embodiment, the organic material preferably comprises fermentation at a temperature of about 15°C to preferably less than about 65°C, at a temperature of about 257 to preferably particles having a length of less than 5 cm, for example, lower than about 55"С, for example, at a temperature of such solid particles having a length of tour from about 35"7С to preferably lower than about less than 1 cm. 4576.

Organic material before its arrival - It is desirable that the fermentation takes place by stretching to the lime treatment unit under pressure for a period of time from about 5 to preferably less than it is desirable to grind, preferably with an auger - 15 days, for example during a period of time from a nearby conveyor , equipped with a shredder, for 7 to preferably less than 10 days. it is better if it is made of stainless steel and One embodiment provides a method where the skin is acid-resistant steel. The conveyor will feed the biogas organization takes place on one or more ny material to the lime treatment unit under the plants by microorganisms, preferably a strain of bacte- pressure, where the organic material needs to be heated, and includes anaerobic fermentation of organics by steam inlet, or steam in a cover around Ag material. During the fermentation of organic regata treated with lime, or any of their compounds, these bacteria produce mainly change. tan and smaller fractions of carbon dioxide. Obtaining

Organic material may also contain pro-biogas may occur on one or more theins or similar organic molecules, including plants by microorganisms, preferably bacterial elements, including amino acids and their com- anaerobic fermentation of organic matter by binations that form prions of sponges of cattle or alu other prions, and where the above-mentioned prions of the bovine spongus In one embodiment, the production of biogas occurs or other prions are removed or destroyed in two plants by bacterial anaerobic indirectly or prepared for destruction by fermentation of organic material, first by a unit of lime treatment under pressure and/or fermentation by thermophilic bacteria on further fermentation, including anaerobic first plant, after which thermophilic enzyme fermentation. The organic material of the animal melted organic material enters the second origin has a high content of nitrogen (M), mainly the plant where fermentation takes place by mesophilic over 10965. them bacteria.

Organic material in the form of liquid manure It is desirable that the thermophilic reaction conditions can be obtained by adding water and/or water include a temperature in the range from 457C to and/or water containing a small concentration of organic- 75"C, for example, a temperature in the range from 5570 night material , preferably less than 10905 to 607. rdy particles. The added water can be recirculated. It is desirable that the conditions of the mesophilic reaction include water, water containing a concentration in the range of 207"C to 45760, organic material obtained from silage, for example, a temperature in the range from 30"C to water, and/or water collected after cleaning 3576. cowshed and washing animals and/or water obtained from fermentation to of the M release process, and/or the reaction took place for about 5-15 days, with water obtained from one or more plants with, for example, during a period of time of about 7-10 biogas production, and/or water obtained under days. during the concentration of phosphorus fertilizers, and/or Possible foaming can be reduced by water obtained during the concentration of potash and/or prevented by adding polymers of these fertilizers, and/or collected rainwater. and/or vegetable oils, and/or one or more

One of the optimal embodiments is the one where water is salt, preferably vegetable oil in the form of rapeseed oil. Salts preferably contain or consist of a cation containing P, can be dried if desired - mainly from CaO and/or Ca(on)". with the aim of obtaining granulate with the content of phos-

Desirable flocculation of substances and particles during fertilizing, for example, biogas production is mainly achieved by introducing the P fraction under a cover or cover, seizing calcium ions capable of forming calcium that allow air to pass through. in the bridges between organic and inorganic sub- Calcium bridges cause the formation of "layers" particles. In addition, the introduction of calcium ions in silage and/or in the process of processing with lime causes the precipitation of orthophosphates, including by pressure and/or in the process of extracting M and/or on biologically with dissolved (PO43). which mainly falls to the Talaba gas plant for cleaning the cowshed in the form of calcium phosphate Саз(РОз4)2, where it is used in the field and/or it is fed to water treatment plants. is in the form of a suspension in liquid manure. Accordingly, this method in another aspect

The obtained biogas is fed to the gas engine, which ensures the production of mainly clean fuel, which is capable of producing heat and/or electrified water, and the above-mentioned production of river current. The heat can be used for heating consists of the following phases i) obtaining from the separation heating of the lime treatment unit under the pressure of the rotor, preferably from the decanting centrifuge, liquid and/or to the fermentation plant and/or to the reaction containing the used water, which has a source of M and/or up to one or more bio-limited content of M and P, preferably less than gas plants and/or premises for keeping Bo (m/u-Weight per volume), for example less than 1 90 animals and/or to human dwellings and/or for (mm), e.g. less than 0.195 (m/u), e.g. heating water for human domestic needs. Vi- less than 0.0190 (m//u), and mainly does not contain generated electricity, it is possible to direct and sell sources of possible spread of zoonoses (diseases, you to commercial electricity supply networks that are transmitted to humans from animals), veterinary diseases. In one optimal embodiment, organic viruses, infectious bacteria, parasites or other material from which is isolated nitrogen, which is sterilized The seeds of infections, including prions of encephalitis, are fermented and transported to the agricultural fields - sponges of cattle and other prions. For some it is a problem. different embodiments are acceptable if used water

In addition to: will contain less than 1095 M and P that were contained in the liquid) Reduction of the amount and/"or removal of some manure at first. desired microorganisms, In another aspect, this invention provides a con- i) Improvement of biogas production, seb production of potassium (K) containing mineral i) Provision of a very convenient to use fertilizer from organic materials with a source of organic material from which potassium is isolated, and the above-mentioned production contains nitrogen, which is sterilized and fermented, i) supply of liquid fractions from the first phase of separation, in another respect, the invention relates to the method of treatment (applied for the separation of phosphorus-receiving M, containing mineral fertilizers from containing organic materials as mentioned above) of organic materials containing a source of M, added to the second phase of separation, i ) separation, why does the above-mentioned production consist of phases: excess organic and inorganic compounds from rii) collection of M, including ammonia extracted from melon, ii) obtaining a solid fraction with a K content, where the organic material in the separation phase is M, the above-mentioned solid fraction is capable of being used- i) absorption of the above-mentioned M, including as a potassium mineral fertilizer, suitable for ammonia in water or an acid solution containing for application to the soil agricultural land as desired. sulfuric acid, The second phase of separation preferably includes pro- ii) obtaining nitrogen mineral fertilizer, passage of the fraction containing potassium through the micro- which can be used in the field. filter operated with alternating aeration

This invention, in yet another aspect, includes the collection and filtration of waste water, where the production of phosphorus (P) containing mineral aeration provides the decomposition of residual fertilizer from organic materials containing jack organic material and the deposition of neorelo P , and the above-mentioned preparation of ganic flakes. from such phases i) supply of liquid manure from biogas In another aspect, this invention provides a fermenter to the separator, i) separation of the production of clean waste water, where fermented organic, as well as inorganic waste water is treated with material into solid and mainly liquid fractions, in an aerobic treatment system capable of removing) obtaining a mainly solid fraction that you and/or reducing the amount of Mi P in water and containing a part of P, preferably in the form of phosphate, it is also desirable to decompose the residual organic calcium Саз(РО»4)2, and organic phosphate in the material and odor components, obtaining a suspension in liquid manure, where the above-mentioned treated water is mainly free from M and P, where the raw fraction can be used as phospho- the above-mentioned waste water is suitable for mineral fertilizer, which can be applied to the soil of agricultural land as desired, or be applied to the fields if necessary. recirculated through the room for maintenance

Separator for separating fermented animals. of organic, as well as inorganic material on The above-mentioned aeration can take place from at- solid and mainly liquid fraction - it is desirable mospheric air for 2-4 weeks at tem- decanting centrifuge. Mostly solid, the temperature is about 207 and the liquid-gas ratio is close to

zko 1:2000. Removed M can be collected and submitted to meat and bone meal, blood plasma, or the like to an absorption column, as described elsewhere in animal products, risks. forged or non-risk material from inspection

By providing the possibility of cleaning the potential presence of cattle spongy prions in market premises treated in this way or other prions, and/or waste water, this invention provides a) third component, preferably a plant with a method of improving energy production in yet another aspect , which produces an increased amount of hygiene of the livestock premises or stables, the amount of energy from biomass containing organic matter, and the above-mentioned improvement consists in the additional material, in which the first component contains: the selected premises obtained by the used a) cleaning system of one or more floors, water Cleaning consists in cleaning and washing stands, pig pens, channels for removing, for example, boxes, floors, stands, channels for manure, channels for the flow of liquid manure, animals, and cleaning manure, ceiling, ventilation channels, ventilation channels of livestock premises and exhaust air from the washing room colony or barn, and the above-mentioned cleaning includes (scrubber), etc., as well as the reduction of emission areas, the use of cleaning water, and/or, from where odor, ammonia and dust can be emitted into p) the cleaning water supply system, not the environment of a specific location - necessarily in the form of liquid manure containing dung, including a cowshed. cleaning water and organic material, from the

The cleaning of the cowsheds in one of the incarnations of the barn or barn to the second is preferably used water, a component in which the second component contains: manna after fermentation of energy-intensive balls a) the first pre-treatment tank, tour or obtained after fermentation for preferably extractable tank for Her) selection M for the performance of biogas separation of solids (nitrogen), including ammonia, from liquid manure, which is wine and liquid or waste water, received from the first component to the second from a later process in the system. component, or iii) allocation of M (nitrogen), including

There is also the possibility, according to this aspect, of ammonia, from the organic material that comes from the invention, to improve the keeping of animals in the piggery by using straw in it, which is the second component, and the first tank gives the animals the opportunity to dig in it and engage in pretreatment it can, optionally, also be used as structural fodder. To be used for hydrolyzing organic matter from embodiments, it is desirable to serve before processing the material, and/or; straw with the content of organic material from p) the second pre-treatment tank, the bas- bin to the unit for processing lime under pressure, the unit for processing lime under pressure and hydrolysis of organic material. Another for the hydrolyzation of liquid manure containing organic - the general purpose of improving the living conditions of animals in the pig- night material that comes from the first cell is the possibility to wash the animals stream- member to the second component, and above water to reduce the number of microorganisms , this hydrolysis causes the destruction, inactivation, and dust in the fur of animals and at the same time lowers and/or decreases the number of any vital signs of the animal's temperature. of microorganisms and/or pathogenic substances,

This method provides a way of integrating present in liquid manure, or their parts, and/or; anaerobic fermentation of animal manure, c) at least one tank, preferably of silage-energy-intensive crops and similar organic sub-tank, for obtaining silage growth, as well as processing nutrients, liquid material containing at least one contained in digested biomass for minerals - or several of the listed materials: corn, flax fertilizers of commercial quality, in combination with energy-intensive agricultural crops, beets and agricultural residues by obtaining clean waste water. cultures, and/or;

The above-described integrated method requires 4) at least a second tank, preferably a system of components, or a selection of such components, a pre-treatment fermentation tank as described in more detail elsewhere in this document for the fermentation of silage and/or organic ment. material treated with lime under pressure, in which

In one aspect, the system consists of: the fermentation conditions are selected from the conditions of mesophilic) the first component, preferably livestock and/or thermophilic fermentation, in which premises or barns for keeping or rearing- the third component contains: animals, preferably domestic animals , including a) at least one biogas fermenter, cows, pigs, cattle, horses, goats, sheep and/or poultry, which may receive liquid manure and/or organic, etc., and/or material from the second component for fermentation and) the second component, preferably at least tation of organic material under the conditions of either a mesophilic pretreatment plant for organic fermentation, or thermophilic fermentation, material, and the above-mentioned organic ma- and the above-mentioned fermentation provides terial consists of animal manure and/or tva - production of biogas with a content of mainly methane, liquid manure and/or plant and/or plant parts, and the aforementioned plant parts p) at least one reserve uar for collection consist of one or more of the listed biogas, and the tank is not necessarily sub-materials: straw, agricultural crops, residues of agricultural crops, nano to the outlet for biogas removal or sub-silos, energy-intensive agricultural crops, and, if desired, nano to a gas engine, and/or; carcasses or parts of animal carcasses, slaughterhouse waste, c) at least one first separator, ba-

a decanting centrifuge, in which the fermentation of the above-mentioned extracted M to the column, in which the material from at least one biogas which M, including ammonia, is absorbed by water or the fermenter is divided into a mainly liquid acid solution, which preferably contains a sulfur fraction in the form of waste water, and into basic acid, and optionally store the absorbed solid fraction, and the above-mentioned solid ammonia in the tank. The water-absorbed or acidic fraction contains solid phosphorus (P) with the content of a lot solution M in this way organic and inorganic material is used, and/or; as a mineral fertilizer. a) at least one second separator, preferably a lime treatment unit under pressure, a systen ceramic microfilter, in which the spent water is preferably a device capable of grinding water from at least one first separator, organic material into particles and capable of further processing, preferably by aeration and feed the crushed organic material through the filter, and the above-mentioned processing to the chamber, where the above-mentioned crushed organic- causes the elimination of at least some, and the desired material is heated and simultaneously exposed to the action of but also the greater part of one or more components- high pressure due to the increase in temperature. of odors, nitrogen compounds (M) and potassium compounds (K), to the organic material processed in the aggregate, and the above-mentioned separation also ensures lime treatment under pressure, lime is added to obtain waste water containing and/or Ca(OH)", before or after a limited amount of one or more components entering the lime treatment unit under the smell, nitrogen compounds (M) and potassium compounds (K) in the pore pressure. considered with the quantity before division. It is advisable to add Sao to the processing unit

The system mainly consists of a pipe-cleaning agent under pressure in the amount of 5-10 g per kg of dry resins, which form a closed system that prevents organic material. The system works to suppress or reduce emissions of one or more below - at a temperature from 1007C to 220"C, for example, the listed substances: dust, microorganisms, 18070 - 2007"C. The temperature is chosen depending on ammonia, air, liquid or any other component of the processed organic material, higher part of the system. the temperature is chosen for the increased content

Liquid fractions or waste water from one cellulose, hemicellulose and lignin in organic or several from at least one silage res- material or a higher temperature is chosen for rvoir, at least one fermentable presence of the risk of the presence of infectious micro-reservoir pretreatment, at least ganisms or pathogenic compounds that include one biogas fermenter, at least bovine spongiform prions in organic material. of the first separator and at least one The pressure is preferably from 2 to less than 16 of the second separator is reused for bar, for example, from 4 to preferably less than 16 bar, cleaning the livestock room or barn. for example, from 6 to preferably less than 16 bar, on-

Liquid fractions or waste water from any example, from 10 to preferably less than 16 bar. Sys- of one or more silage tanks, each subject is operated at an elevated temperature of at least one fermentation tank for 5-10 minutes, but pre-treatment, at least one and longer treatment periods can be used. of the biogas fermenter, at least one M, including ammonia, extracted in the first separator unit and at least one second lime treatment under pressure, collected and fed to the separator is reused in any to the column, and absorbed as described in other mis- phase systems for separation of liquid manure and by-products. biogas to maintain organic material The system in one embodiment facilitates in the proper liquid state. feeding of silage, for example, from corn, energy

The system makes it possible to add lime, which contains CaO and/or Ca(OH)" to the organic materials, thermophilic or mesophilic tank before the above-mentioned organic fermentation takes place. before further feeding the mined material to the extraction tank for the material to the extraction tank. release of M, including ammonia, preferably by The system may also facilitate the addition of an amount of lime sufficient to pressure lime-treated organic mate- baking pH from about 10 to about rial to a tank of thermophilic or mesophilic- 12, optionally in combinations with a heating phase of fermentation before further feeding and aeration of liquid manure, including organic material, to the extraction tank. material. The system can also facilitate optimization

Organic material is in the extraction and fermentation of organic material and the resulting tank of the system for 5-10 days, for biogas by providing means, including example, 7 days. The temperature inside the pre-treatment unit for the wine tank is extracted in the optimal version of division M, including ammonia, and/or execution is from 60"C to 80"C. Approximately 30-60g of alkaline hydrolysis with the given technological pa-

Ca(on)": per kg of dry matter in organic mater- meters, which include the pH level, temperatures are added to the organic material in extraction, aeration, duration, braking in the foaming tank or before the arrival of rise and flocculation suspended material. of the mentioned organic material to the minable system in another variant of its implementation of the storage tank. hears optimized conditions for the population of microorganisms

The system facilitates the selection of extracted M, including those contained in fermenters for obtaining ammonia, from the extraction tank and feed biogas. This is achieved, for example, by supplying sterilized or sanitized liquid treated water from the first separator in the second manure from the extraction tank to at least one separator, and the above-mentioned second separator- the first biogas fermenter, and the above-mentioned separator has ceramic microfilters in which the processed sterilized or sanitary treated water from the first separator, additionally cleaned liquid manure does not interfere with and does not harm the microorganisms that produce biogas in the fermen- by aeration and filtration, without necessarily removing any remains of the computer. In particular, organic material from which the odors, any residues of nitrogenous compounds and M with ammonia content can be fed to the bio- any components containing K (potassium), a gas reactor, in which the conditions fermentation using clean waste water, which mainly promotes mesophilic fermentation. If the organic material does not contain any of the above-mentioned residual compounds, the material entered the mesophilic enzyme. tion, then the organic material is fed to another The system also makes it possible to feed ref- biogas reactor of the system, in which the conditions of fer- ferred water from thermophilic biogas reaction favor thermophilic fermentation. tor to the field, to water treatment facilities or to treatment

Thermophilic fermentation conditions include a plant, or a biological treatment plant reaction temperature ranging from about 457C for further purification as desired. to 75"C, for example, include a reaction temperature in the range from about 557C to 60"C. Conditions to use for: mesophilic fermentation include temperature - Prevention or reduction of emissions in the reaction in the range from about 207C to 457C, environment of dust, microorganisms, ammonia - example, include reaction temperature within ku, contaminated air, liquid or other formation from approximately 30"С to 3576. renation within the system, in particular, indoors

The system makes it possible to perform as ter- for keeping animals. mophilic and mesophilic reaction during the period of at least 5-15 days, for example, during tities in the biomass of organic material. about a minimum of 7-10 days, in an optimal way - Improving the production of biogas, which is a minimum of 7 days. methane gas and methane carrier gas. The above-

The system includes means capable of preventing foamy gas can be stored in a tank at the site of new formation, and the above-mentioned means are capable and/"or sold to commercial networks that introduce, for example, polymers and/or vegetable oils, supply it to consumers. including rapeseed oil, and/or various salts, including - Obtaining separate fractions of M (nitrogen), P containing salts with the content of Сас and/or Са(ОНН)» (phosphorus) and possibly K (potassium) from organic materials

The system makes it possible to reuse materials. The above-mentioned fractions should consume at least part of the fermented organic value and can be used as mineral material from biogas reactors in the form of fertilizers for application to the soil of the field/garden. my reactor, and the above-mentioned - Ensuring improvement of the conditions of keeping fermented organic material serves inoc- animals and hygiene in animal barns, and in accordance with the summer for the population of microorganisms that carry out- products from the above-mentioned animal barns. Fermentation takes place. the aforementioned products consist of the usual

The system in one version of its embodiment gives mo- animal manure, liquid manure (redote) and animals, the ability to feed liquid manure, which includes liquid intended for slaughter. For clean animals with the content of solid particles, before the first separation, there is a risk that after their slaughter there will be a recipient for the separation of solid materials, including infected meat. including a limited liquid fraction, from the main time- - Ensuring the procedure for processing the liquid fraction of the thread. The above-mentioned mainly half animals or their parts, meat and bone meal solid fraction contains organic and inorganic or other substances of animal origin, which material, including P (phosphorus) and its compounds. makes them suitable for introduction into the soil of agriculture

The above-mentioned mainly solid fraction can be applied to the land in the form of refined mineral fertilizers and then dried and it contains mineral fertilizers - in this way, obtaining benefits from micro and macro. It is desirable that the first separator of the nutrient system of animal origin should be a decanting centrifuge. water from the production of goods for agriculture or

The system also makes it possible to clear plantations.

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Ministry of Education and Science of Ukraine

State Department of Intellectual Property, str. Urytskogo, 45, Kyiv, MSP, 03680, Ukraine

SE "Ukrainian Institute of Industrial Property", str. Glazunova, 1, Kyiv - 42, 01601