RU2015123832A

RU2015123832A - INTEGRATED DEVICE FOR COMPLETE PROCESSING OF HOUSEHOLD WASTE AND PRODUCT METHOD

Info

Publication number: RU2015123832A
Application number: RU2015123832A
Authority: RU
Inventors: Вэньцзи СЮЙ; Квок син ЛИ; Хон син ЛИ; Чунь син ЛИ
Original assignee: Саус Чайна Реборн Ресоурсес (Чжун Шань) Ко., Лтд.
Priority date: 2012-11-23
Filing date: 2013-02-16
Publication date: 2017-01-10
Also published as: CN103056151A; WO2014079173A1; CN203128526U; WO2014079168A1; HK1180657A1; HK1180714A1; CN103071666B; CN203124394U; WO2014079166A1; CN103055650A; CN103074131A; CN103056151B; KR20150105299A; HK1180761A1; WO2014079165A1; WO2014079135A1; CN103056022A; CN103072726B; CN103084049A; CN103071666A

Claims

1. A system for the complete processing of household waste, including an apparatus for cutting packages with household waste, an apparatus for general screening of household waste, an apparatus for liquid oxidation, deodorization, inactivation, purification and reduction of salt content, a vertical apparatus for dehydration, an apparatus for grinding material and apparatus for automatic control, while household waste is placed in the apparatus for cutting packages with household waste and then served in the apparatus for the general screening of household waste, subjected to Ningu a mixture of oil, water and solids is fed into the apparatus for liquid oxidation, deodorization, inactivation, purification and reduction of salts for inactivation, household waste subjected to inactivation, deodorization, desalination and dehydration using liquid oxidation are sent to the apparatus for dehydration using a conveyor pipeline with a threaded rod, the material subjected to dehydration using a dehydration apparatus is fed into the apparatus for grinding material for grinding, an apparatus for automatically It controls other devices.

2. A system for the complete processing of household waste according to claim 1, characterized in that the cutting apparatus includes a horizontal cylindrical housing (D11), one end of the housing (D11) is an outlet (D18), several cutting elements (D12) are fixed on the inside the wall of one end of the outlet (D18) of the housing (D11), inside the other end of the housing (D11) is a piston (D13) that can slide along the internal cavity of the housing (D11) and connected to a drive tool (D12) pushing the piston (D13), on the piston surface (D13) ra cutting grooves (D14) corresponding to each cutting element (D12) are arranged, a loading hole (D21) is located in the middle part at the top of the housing (D11).

3. A system for the complete processing of household waste according to claim 2, characterized in that a roller (D15) is installed in the lower part of the piston (D13), the guide in the form of a recess (D17) is rigidly fixed in the lower part of the inner wall of the housing (D11) in accordance with with the position of the roller (D15), the roller (D15) is able to slide back and forth along the guide in the form of a recess (D17).

4. A system for the complete processing of household waste according to claim 2, characterized in that the collection tank (D19) is installed at the loading opening (D21), the upper part of the collecting tank (D19) has the shape of a funnel, the lower part is connected to the loading opening (D21) on the body (D11) with a pipe (D20), on the pipe (D20) there is a pneumatic slide valve (D27).

5. A system for the complete processing of household waste according to claim 2, 3 or 4, characterized in that the rotary valve (D22) is installed at the outlet (D18) on the body (D11), the motor (D28) rotates the rotary valve (D22).

6. A system for the complete processing of household waste according to claim 5, characterized in that the rotary valve (D22) is square or rectangular and has an internal cavity.

7. A system for the complete processing of household waste according to claim 6, characterized in that each side of the rotary valve (D22) has several holes for pumping air (D23), a channel for compressed air (D24) and a nozzle are located inside the rotary valve (D22) (D26), the nozzle (D26) is connected to the channel for compressed air (D24), the direction of air movement in the nozzle (D26) coincides with the direction of movement in the outlet.

8. A system for the complete processing of household waste according to claim 7, characterized in that the air injection holes (D23) are arranged in parallel.

9. A system for the complete processing of household waste according to claim 2, 3 or 4, characterized in that the blade of the cutting element (D16) is located at an angle of 90 degrees relative to the sectional plane of the outlet of the housing or at an angle of 30 degrees relative to the inner wall of the housing.

10. A system for the complete processing of household waste according to claim 1, characterized in that the apparatus for general screening of household waste includes a housing (E11), a separation plate (E25) is located inside the housing (E11), the inside of the housing (E11) is divided into air zone (E10) and airless zone (E32) with a separation plate (E25), a hole for material (E26) is located on the separation plate (E25), a loading hole is located in the air zone (E10), in the lower part of the air zone (E10) located outlet for heavy material (E 22), the outlet for heavy material (E22) is equipped with a valve (E23), around the outlet for heavy material (E22) there are several air nozzles (E24), in the upper part of the air zone (E10) there are rotating elements with teeth (E30) , inside the airless zone (E32) there is a device for removing material (E33), one end of the device for removing material (E33) is located in the case (E11), the other end is located on the outside of the case (E11), inside the device for removing material (E33) ) a screw is located (E37), a device for Material removal (E33) is equipped with a motor (E36) and transmission (E34), the motor rotates the screw (37) through the transmission.

11. System for the complete processing of household waste according to claim 10, characterized in that the material hole (E26) is equipped with a guide valve (E27), a guide valve (E27) is connected to a pneumatic push-pull rod (E28), the pneumatic device (E38) moves push-pull rod (E28), push-pull rod (E28) controls the opening and closing of the slide gate (E27).

12. The system for the complete processing of household waste according to claim 10, characterized in that the number of rotating elements with teeth (E30) is two, while two rotating elements with teeth (E30), which are located at the top and bottom, half of the lower rotating element with the teeth are located at the liquid level in the air zone (E10), the upper rotating element with teeth is located above the liquid level in the air zone (E10), two rotating elements with teeth (E30) are engaged.

13. The system for the complete processing of household waste according to claim 12, characterized in that on the housing (E11) there is a motor of rotating elements with teeth (E39), the motor of rotating elements with teeth (E39) simultaneously rotates two rotating elements with teeth (E30) .

14. System for the complete processing of household waste according to any one of paragraphs. 10-13, characterized in that the transmission (E34) is installed next to the device for removing material (E33), the motor (E36) rotates the screw (E37) through the transmission (E34).

15. System for the complete processing of household waste according to any one of paragraphs. 10-13, characterized in that the apparatus for automatic control of liquid (E29) for monitoring the level of liquid is installed in the air zone (E10).

16. System for the complete processing of household waste according to any one of paragraphs. 10-13, characterized in that a pipe for transporting household waste into the housing (E11) is installed on the housing (E11), the pipeline is connected to the inlet pipe (E20).

17. System for the complete processing of household waste according to any one of paragraphs. 10-13, characterized in that the inlet for circulating water in the air zone (E10) is connected to a hydraulic booster pump (E21), the water source is provided by the tank for storing circulating water, in the middle and lower parts of the airless zone (E32) there are outlet openings for water, water enters the tank for storing circulating water using a water pump used to circulate water in the air (E10) and airless zone (E32) and to enhance water drilling in the air zone (E10).

18. A system for the complete processing of household waste according to claim 1, characterized in that the apparatus for liquid oxidation, deodorization, inactivation, purification and reduction of salt content includes several reactors (F34) and a device for mixing gas, water and material (F42) for mixing ozone, water and material, the mixing device (F42) is connected to a waterproof non-return valve, one end of the waterproof non-return valve after connecting to the gas pipe is connected to an ozone producing device (F44), a mixing device (F42) It is also connected to the outlet of the cam rotary pump for high viscosity material (F49), the outlet of the mixing device (F42) passes to the reactor (F34), the inlet of the cam rotary pump for material with high viscosity (F49) is connected to another reactor ( F34), inside the reactors (F34) there are several elements with granular activated carbon (F41), elements with granular activated carbon (F41) contain granular activated carbon, the material outlet is located in bottom of each reactor (F34).

19. The system for the complete processing of household waste according to claim 18, characterized in that the total volume of granular activated carbon is 15% -98% of the volume of the spherical cavity of elements with granular activated carbon (F41).

20. A system for the complete processing of household waste according to claim 18, characterized in that the automatic exhaust valve (F38) is located at the top of each reactor (F34), the automatic exhaust valve (F38) is connected to an ozone destruction device (F39).

21. The system for the complete processing of household waste according to paragraphs. 19-20, characterized in that the semicircular lid (F35) is located at the bottom of each reactor (F34), the material outlet is located on the semicircular lid (F35).

22. System for the complete processing of household waste according to paragraphs. 19-20, characterized in that the most forward reactor (F34) of the reactors (F34) is equipped with an inclined conveyor with a helical belt (F36), and the farthest reactor (F34) is equipped with a pipeline for regulating the water level.

23. System for the complete processing of household waste according to paragraphs. 19-20, characterized in that the hole for removing material is connected to a device for separating solids and liquids.

24. System for the complete processing of household waste according to claim 23, characterized in that the device for separating solids and liquids includes a housing (F45) and an inclined mesh drum (F52), an inclined mesh drum (F52) is located in the housing (F45), the motor rotates the inclined mesh drum (F45) through the transmission, several rows of holes are located in front of the inclined mesh drum (F52), inside the inclined mesh drum (F52) there is a screw tape connected to the inner wall of the inclined drum, the water collector (F47) is located wives in the bottom of the housing (F45).

25. System for the complete processing of household waste according to claim 24, characterized in that the helical tape is located along the entire length of the inclined mesh drum (F52).

26. System for the complete processing of household waste according to claim 24, characterized in that the housing (F45) is provided with a window (F46).

27. System for the complete processing of household waste according to paragraphs. 18-20, characterized in that the sides of the reactors (F34) are provided with inspection openings.

28. System for the complete processing of household waste according to claim 1, characterized in that the vertical dehydration apparatus includes a housing (G49), a vertical supply column (G50) and a pusher with screw tapes (G51), a vertical supply column (G50) is located inside housings (G49), a pusher with screw tapes (G51) is located inside the vertical supply column (G50), on the sides of the vertical supply column (G50) there are several outlet openings (G58), the loading hole (G62) is located at the bottom of the vertical supply columns (G50), the outlet (G60) is located in the upper part of the vertical supply column (G50), in the lower part of the casing (G49) there is a drive that rotates the pusher with screw tapes (G51), inside the casing (G49) on four sides of the lower parts of the vertical supply column (G50) are located water traps (G55), water traps (G55) are connected to the holes for water outlet (G63).

29. A system for the complete processing of household waste according to claim 28, characterized in that several water pipes (G65) are located inside the housing (G49) and around a vertical supply column (G50), each water pipe (G65) is connected to several holes for high pressure water (G53).

30. A system for the complete processing of household waste according to claim 28 or 29, characterized in that a retainer plate (G61) of the pusher with screw tapes (G51) is installed in the upper part of the vertical supply column (G50).

31. The system for the complete processing of household waste according to Claim 30, characterized in that a sealing cover is installed at the end of the screw tape on the pusher with screw tapes (G51) to regulate the discharge rate.

32. A system for the complete processing of household waste according to claim 28 or 29, characterized in that the screw pitch of the screw tapes on the pusher with screw tapes (G51) gradually narrows in the direction from the bottom to the top.

33. The system for the complete processing of household waste according to claim 32, characterized in that the screw pitch in the lower parts of the screw tapes on the pusher with screw tapes (G51) is 25 cm and 10 cm in the upper part.

34. A system for the complete processing of household waste according to claim 28 or 29, characterized in that the drive includes a motor (G54), a transmission (G64) and a rotary converter (G66) that converts horizontal axial rotation to vertical axial rotation, motor ( G54) rotates the transmission (G64), the transmission (G64) rotates the rotary converter (G66), the rotary converter (G66) rotates the pusher with screw bands (G51).

35. A system for the complete processing of household waste according to claim 28 or 29, characterized in that a stainless steel support sleeve (G56) is located inside the housing (G49).

36. System for the complete processing of household waste according to claim 28 or 29, characterized in that there are several vertical stainless steel plates (G56) around the outer surface of the vertical supply column (G49), and several vertical stainless steel plates (G56) are located reinforced traps, on each reinforced trap there is an inclined recoil overhang.

37. System for the complete processing of household waste according to Claim 28 or Clause 29, characterized in that the vertical supply column (G49) consists of several columns, the upper and lower annular parts of each column have reinforced flanges, the joints between adjacent columns are butt connections between the upper and lower flanges of the columns, which are fixed by bolts, the upper flange in the area of the connection of the flanges of each column has an inclined recoil overhang.

38. The system for the complete processing of household waste according to claim 1, characterized in that the apparatus for biochemical fermentation includes an anaerobic fermentation tank (I65) and a primary fermentation apparatus (I70), the primary fermentation apparatus (I70) includes two secondary fermenters (I71) and several primary fermenters, two secondary fermenters (I71) are located above the primary fermenters, feed holes (I84) are located at the junction of the secondary fermenters (I71) with the primary fermenters, inside the primary fermentation apparatus p a material elevator (I64) was installed for feeding material to the secondary fermenters (I71), stirring devices (I73) are located inside the secondary fermenters (I71), mixers with double-layer screw tapes (I78) are located inside the primary fermenters, anaerobic fermentation tank (I65) connected to the primary fermenters, the anaerobic fermentation tank (I65) feeds the material to the primary fermenters using an automatic loading system (I67).

39. The system for the complete processing of household waste according to claim 38, characterized in that each mixer with two-layer screw tapes (I78) includes a shaft, an internal screw tape and an external screw tape, an internal screw tape located inside the external screw tape, an internal screw tape and the outer screw tape is a screw tape and is rigidly fixed to the shaft, the directions of rotation of the inner screw tape and the outer screw tape are opposite, around the shaft of each mixer with double-layer screw Tammy (I78) added vane (I79).

40. A system for the complete processing of household waste according to claim 38 or 39, characterized in that a shaft is located in the middle of each stirrer (I73), several stirring blades are rigidly fixed on the central shaft.

41. A system for the complete processing of household waste according to claim 38 or 39, characterized in that in the upper part of the anaerobic fermentation tank (I65) there is a mixer for material (I68), which can move automatically.

42. A system for the complete processing of household waste according to claim 1, characterized in that the automatic unloading multi-stage drying apparatus includes a pre-drying device (J93) and a main drying device, a pre-drying device (J93) is installed above the main drying device, the device case for preliminary drying (J93) is two-sided, a multilayer cavity (J97) is formed between the two sides in the housing, an automatic blade for ma is located inside the device for preliminary drying (J93) series (J94), in the middle of the main drying device there is a horizontal cylinder (J102) that can rotate counterclockwise and clockwise 360 degrees, the front and rear ends of the main drying device are fixed elements (J101), inside the horizontal cylinder (J102 ) there are several secondary drums that are rigidly fixed on the horizontal cylinder (J102), inside the horizontal cylinder (J102) and the corresponding secondary drums there are material guiding screw tapes, on There is a gas or liquid fuel combustion chamber (J99) and a burner (J100) located in the drying oven, the heat received through the burner (J100) enters the main drying apparatus, the tail gas of the main drying apparatus enters the multilayer cavity in the housing (J97) through the hot air removal (J107), a hole for removing material of the pre-drying device (J93) is located at the innermost secondary drum of the main drying device.

43. The system for the complete processing of household waste according to claim 42, characterized in that in the lower part of the pre-drying device (J93) there is an automatic unloading device with a screw in the form of a screw tape (J95), an automatic unloading device with a screw in the form of a screw tape (J95) is cylindrical and has a screw-type screw inside.

44. The system for the complete processing of household waste according to claim 42, characterized in that in the upper part of the pre-drying device (J93) there is an air supply device (J98).

45. System for the complete processing of household waste according to paragraphs. 42-44, characterized in that the respective secondary drums are installed nested, and the holes for feeding material of the external secondary drums are longer than the holes for removing material of the inner secondary drums.

46. System for the complete processing of household waste according to paragraphs. 42-44, characterized in that on the outer side walls of the respective secondary drums air blades are rigidly fixed (J103).

47. System for the complete processing of household waste according to paragraphs. 42-44, characterized in that the material-guiding screw tapes inside the horizontal cylinder (J102) and the corresponding secondary drums have a different direction.

48. A system for the complete processing of household waste according to claim 1, characterized in that the material sorting apparatus includes a base (K108), a metal rotating mesh pipe (K110), a material conveyor (K113), an automatic conveyor device (K114), chain conveyor (K115) and bypass air valve (K116), a metal rotating mesh pipe (K110) is installed on the base (K108), a material conveyor (K113) is located below the metal rotating mesh pipe (K110), an automatic conveyor device (K114) is located below tr Material conveyor (K113), in the front of a metal rotating mesh pipe (K110) there are openings in the form of cells, a screw tape is located in its rear part, a chain conveyor (K115) is located below the outlet of a metal rotating mesh pipe (K110), an air bypass a valve (K116) is located at the tail end of the chain conveyor (K115).

49. The system for the complete processing of household waste according to claim 48, characterized in that each of the openings in the form of cells has a diameter of from 4 mm to 6 mm, the openings in the form of cells are located at a distance of 2 mm.

50. The system for the complete processing of household waste according to claim 48, characterized in that the metal rotating mesh pipe (K110) is located at an angle, the angle of inclination is from 1 degree to 20 degrees.

51. The system for the complete processing of household waste according to paragraphs. 48-50, characterized in that the bypass air valve (K116) is equipped with a control apparatus for regulating the height of the bypass air valve (K116) relative to the chain conveyor (K115), on one side of the bypass air valve there is a pneumatic switching device.

52. System for the complete processing of household waste according to paragraphs. 48-50, characterized in that on the outer side of the metal rotating mesh pipe (K110) is a protective housing (K109).

53. The system for the complete processing of household waste according to claim 1, characterized in that the apparatus for general screening of household waste has an end for removing hard plastic, an end for removing hard plastic of an apparatus for general screening of household waste is connected to an apparatus for processing plastic waste.

54. The system for the complete processing of household waste according to claim 53, characterized in that the apparatus for processing plastic waste generally includes a main apparatus for processing, the main apparatus for processing transports the material to a pneumatic automatic feeding device (M123) using a conveyor belt ( M122), the material is transported to a cracked catalytic horizontal reaction boiler (M124) using a pneumatic automatic feed device (M123), the reaction boiler (M124) can rotate clockwise and counterclockwise 360 degrees, inside the reaction boiler (M124) there is an automatic device for arbitrary rejection (M125), the reaction boiler (M124) is connected to an external vacuum system (M130), the reaction boiler (M124) is connected to a paraffin-oil separator (M129) ) by means of a pipeline, a non-return valve (M128) is located on the pipeline, the paraffin-oil mixture separator (M129) is connected to the first stage heavy oil separator (M131) by the pipeline, the first stage heavy oil separator (M131) is connected to the first condenser stage (M132) by means of a pipeline, the lower part of the first stage condenser (M132) is connected to the oil container (M133), the rear part of the first stage condenser (M132) is connected to the negative pressure generating device (M134), the back of the negative pressure generating device ( M134) is connected to a vertical gas tank with a water lock (M135), the lower part of a vertical gas tank with a water lock (M135) is connected to a secondary gas compressor (M136), a secondary gas compressor (M136) is connected to a gas storage (M137).

55. System for the complete processing of household waste according to claim 54, characterized in that a cracking furnace (M126) is located in the lower part of the reaction boiler (M124), the outlet pipe of the cracking furnace (M126) is connected to the tail gas treatment system for protection environment (M127).

56. System for the complete processing of household waste according to claim 54, characterized in that the oil container (M133) is connected to a decarburization cleaning device (M139) and a device for dewaxing and dehumming (M140).

57. The system for the complete processing of household waste according to claim 53, characterized in that the system also includes an apparatus for processing untreated carbon black, an apparatus for processing untreated carbon black connected to an opening for removing sediment from the apparatus for processing plastic waste.

58. The system for the complete processing of household waste according to claim 57, characterized in that the apparatus for processing untreated carbon black includes a unit for artificial aging of untreated carbon black (N144), a unit for artificial aging of untreated carbon black (N144) is connected to a unit for physical aging (N145), a device for physical aging (N145) is connected to a device for sorting material (N146) using an automatic conveyor device, a device for sorting material (N146) is connected to an automatic quantitative loading device for liquids and solids (N147), at the rear end of the material sorting device (N146) there is a multilayer push-pull threaded rod (N148), the rear end of the multilayer push-pull threaded rod (N148) is connected to the device to produce clean, low sulfur, environmentally friendly coal with a high energy content (N149).

59. The system for the complete processing of household waste according to claim 1, characterized in that the system also includes an apparatus for producing biodiesel without distillation, the corresponding apparatus first separates the mixture of water and oil into a mixture of oil, water and solids using a pipeline, then the mixture after separation of oil and water is sent to the apparatus for the production of biodiesel without the use of distillation.

60. System for the complete processing of household waste according to claim 59, characterized in that the apparatus for producing biodiesel without distillation includes a horizontal device with a screw tape for separating solids and liquids (O151), a column for separating oil and water (O152) , an oil storage container (O149), a homogenizer (O158), an exchange device (O161) for thick oil fractions operating at room temperature, a liquid separation device (O172) and a filter device (O173), the outlet of the device from the mountains an umbrella screw tape for separating solids and liquids (O151) is connected to the middle lower end of the oil and water separation column (O152) using a pipeline, inside the oil and water separation column (O152) there is a heating pipe (O153), a heating pipe ( O153) extends into the oil and water separation column (O152) from the bottom of the oil and water separation column (O152) and exits the oil and water separation column (O152) from the middle upper part of the oil and water separation column ( O152) in An oil scraper (O155) is located on the top of the oil and water separation column (O152), the oil and water separation column (O152) is connected to the oil storage container (O149) through an oil outlet pipe (O156), an oil inlet outlet pipe inlet (O156) is located at the oil scraper (O155), while the oil storage container (O149) is connected to the homogenizer (O158) through a pipeline, the baffle plate with holes (O159) is rigidly fixed inside the homogenizer (O158), in the corresponding parts on both sides of the baffle plate plate (O159) mouth hydraulic pushing screws (O160) have been updated, hydraulic pushing screw blades (O160) are located in the homogenizer (O158), the motor is located on the outside of the homogenizer (O158), the motor rotates the blades, an outlet for thick oil fractions is installed at the bottom of the homogenizer (O158), the hole for thick fractions of oil is connected to the exchange device (O161) for thick fractions of oil operating at room temperature using a pipe inside the exchange device (O161) for thick fractions of oil working at room temperature re, there are several ultrasonic generators (O162), in the upper part of the exchange device (O161) for thick oil fractions working at room temperature, there is a loading hole (O169), the lower part of the exchange device (O161) for thick oil fractions working at room temperature temperature, is connected to a liquid separation device (O172) by means of a pipeline, while the lower part of a liquid separation device (O172) is connected to a filtering device (O173) by an oil pipe, while at the outlet the filter of the driving device (O173) receive biodiesel.

61. System for the complete processing of household waste according to claim 60, characterized in that the horizontal device with a screw tape for separating solids and liquids (O151) includes a horizontal cylindrical body, a strainer is located inside the housing, a conveyor screw is rigidly fixed inside the strainer , the screw tape is connected to the motor through a transmission for rotating the screw tape and strainer, at the bottom of a horizontal device with a screw tape for separating solids and liquids (O151) a conduit is located for discharging a mixture of oil and water.

62. The system for the complete processing of household waste according to claim 60, characterized in that an infrared water level sensor (O154) is located at the top of the oil and water separation column (O152).

63. System for the complete processing of household waste according to Claim 60, characterized in that a housing (O163) is installed around each ultrasonic generator (O162), internal holes (O164) are located around the housing (O163), the locking device (O165) is rigidly fixed over housing (O163), an ultrasonic generator (O162) is installed in an exchange device (O161) for thick oil fractions operating at room temperature using a shut-off device (O165).

64. System for the complete processing of household waste according to claim 60, characterized in that the exchange device (O161) for thick oil fractions operating at room temperature contains a pipe for draining the liquid (O166), one end of the pipe for draining the liquid (O166) connected to the upper part of the exchange device (O161) for thick oil fractions operating at room temperature, the other end is connected to the lower part of the exchange device (O161) for thick oil fractions operating at room temperature, the pipe for draining the liquid (O166) is connected Strongly pump (O167).

65. The system for the complete processing of household waste according to claim 60, characterized in that in the lower part of the exchange device (O161) for thick oil fractions operating at room temperature there is a blower pipe (O171), one end of the blower pipe (O171) is connected with installation for compressed air.

66. The system for the complete processing of household waste according to claim 60, characterized in that the system also includes a homogenizer, the oil mixture is supplied from the oil storage container to the homogenizer using a special oil pump and then enters the exchange device for thick oil fractions.

67. The system for the complete processing of household waste according to claim 66, characterized in that the system also includes an apparatus for the production of emulsified biodiesel, and after the exchange device for thick fractions of oil, the oil mixture enters the apparatus for the production of emulsified biodiesel.

68. The system for the complete processing of household waste according to claim 67, characterized in that the apparatus for the production of emulsified biodiesel includes a housing (P174), a housing (P174) contains a vertical mixer (P175), the engine rotates a vertical mixer (P175), on the central several vertical impellers in the form of blades (P178) or impellers in the form of blades are installed on the shaft of the vertical mixer (P175), a turbine or curved circular blade (P179) is installed in the lower part of the central shaft of the vertical mixer (P175), installed in the upper part of the body (P174) but the nozzle for spraying oxygen-enriched water (P185), in the upper part of the body (P174) there are several loading holes (P181), each loading hole (P181) is connected to the quantitative loading device (P182) via a pipe, on one side of the middle upper part housing (P174) there is an oil inlet hole (P192), which is connected to the oil pump via a pipeline, an inlet pipe (P186) is located in the upper part of the housing (P174) and connected to a high pressure pump (P187), a water source is inlet m pipe (P187) is provided a tank for storing oxygen enriched water (P191), from oxygen-rich water is released O ₃ as a gas through the ozone generator (P188) and then proceeds in a powerful device for the mixing of gas and water through the conduit for gas and Incoming it enters the water through the mixing pipeline (P190) into the storage tank for oxygen-enriched water (P191), in the lower part of the casing (P174) there is an opening for removing the finished product (P184).

69. The system for the complete processing of household waste according to claim 68, characterized in that the upper part of the body (P174) is cylindrical and the lower part is semicircular.

70. A system for the complete processing of household waste according to claim 69, characterized in that several plates for water drainage are installed around the cylindrical inner walls of the housing (P174).

71. A system for the complete processing of household waste according to claim 69, characterized in that a support bracket (P180) is installed in the lower part of the housing (P174) to support the rotating shaft of the vertical mixer (P175).

72. System for the complete processing of household waste according to any one of paragraphs. 68-71, characterized in that the drive includes a motor (P176) and a speed control device (P177), while a speed control device (P177) is installed in the upper part of the housing (P174), the motor (P176) is located above the control device speed (P177), while the motor (P176) rotates the vertical stirrer (P175) through the speed control device (P177).

73. The system for the complete processing of household waste according to claim 1, characterized in that the system also includes an apparatus for the rapid processing of wastewater, while the wastewater produced by the apparatus enters the apparatus for the rapid processing of wastewater through pipelines.

74. The system for the complete processing of household waste according to claim 73, characterized in that the apparatus for the rapid treatment of wastewater includes a wastewater filtration tank (Q185), a barrier for solid waste (Q185) is located inside the wastewater filtration tank (Q185) , inside the solid waste barrier (Q185) there is a device for eliminating unpleasant odors (Q187), a wastewater filtration tank (Q185) is connected to a device with a hot plate for wastewater treatment (Q188) using a pipeline, a device with a hot plate A wastewater treatment plant (Q188) includes an internal cavity (Q189) and a housing (Q190), in the upper part of the housing (Q190) there are many sprayers (Q192) connected to the pipeline, a hot plate (Q193) is installed below the sprayers (Q192), inside the hot plate (Q193) there is a heat-conducting oil pipe (Q195), under the lower part of the hot plate (Q193) there is a zone for deposition of microscopic solid particles (Q196), in the lower part of the zone for deposition of microscopic solid particles (Q196) there is an outlet for sewage water outlet (Q197), above the sewage outlet (Q197) there is a valve against the backward flow of liquid to eliminate unpleasant odors (Q198), below the hot plate (Q193) there is a heat-resistant shock-absorbing surface (Q199) to support the hot plate (Q193), in the upper part of the casing (Q190) there is a valve for automatic suction and discharge (Q200), in the casing (Q190) above the hot plate (Q193) there is a hole for collecting hot steam (Q201), a hole for collecting hot steam (Q201) is connected to the heat exchanger (Q202) with the help of the cable, the rear end of the heat exchanger (Q202) is connected to the collection tank (Q203), the collection tank (Q203) is connected to the oxidizing system (Q204) via a pipeline, the oxidizing system (Q204) has two cavities, namely the inner and outer cavities, the inner cavity is a reaction chamber for converting gas into water (Q205), the outer chamber is a supporting reaction circulation chamber for converting gas into water (Q206), at the end of the inlet pipe at the water inlet of the inner cavity there is an activated carbon coping (Q209), activated carbon element (Q209) contains granular activated carbon, a waste water outlet (Q212) is located in the lower part of the internal cavity, a waste water outlet (Q212) is connected to the waste water outlet (Q213) on the casing, at the outlet for sewage (Q212) of the internal cavity, a valve against the backflow of liquid (Q214) is also installed, the oxidation reactor is connected to a device for mixing gas and water (Q215) through a circulation pipe, The gas and water mixing device (Q215) has a T-shaped connection, the two ends are connected to the circulating water, the hole in the middle is connected to the moisture-proof check valve (Q216), the other end of the moisture-proof check valve (Q216) is connected to the gas pipe of the ozone generator, oxidizing the system (Q204) is connected to the intermediate reservoir (Q218), the intermediate reservoir (Q218) is connected to the activated carbon filtering fixed bed (Q219), the activated carbon filtering fixed layer (Q219) is connected to the composite filter filter device (Q220), a composite filter device (Q220) includes several filter tanks (Q221), several vertical filter columns (Q222) are located in the filter tanks (Q221), an outlet for water is located in the middle of each vertical filter column (Q222), in the lower part of each vertical filter column (Q222) there is a mesh filter with 80-140 cells, in the upper part of each filter tank (Q221) there is a water inlet (Q223) and a sealed pipe (Q224), the housing of each filter the tank (Q221) is divided into two halves, in each half of the filter tank there is a stand for filter columns (Q226), on the stand for filter columns (Q226) there are holes whose diameter is equal to the diameter of the filter columns (Q222), filter columns (Q222) inserted into the stand for filter columns (Q226), an inlet pipe (Q228) is located on one side of the upper part of the upper half of the tank, an inlet pipe (Q228) leads to the upper part of the lower half of the tank body, on one side of the lower part of the upper half of the tank an exhaust pipe is located (Q229), an exhaust pipe (Q229) leads to the lower part of the lower half of the tank body, an outlet is located on one side of the upper and lower half of the tank (Q230), the outlet openings of the filter tanks (Q221) are located on one side (Q233) the bottom of the composite filter device (Q220), in the middle of the bottom is the outlet for the sediment (Q234).

75. The system for the complete processing of household waste according to claim 74, characterized in that on the surface of the hot plate (Q193) there are many shallow grooves for flowing water (Q194).

76. The system for the complete processing of household waste according to claim 74, characterized in that in the upper part of the inner cavity there is an automatic exhaust valve (Q207) and a control liquid level sensor (Q208) for monitoring the liquid level.

77. The system for the complete processing of household waste according to claim 74, characterized in that the upper part of the activated carbon element (Q209) is impermeable, and the lower part is a mesh hole for water (Q210).

78. The system for the complete processing of household waste according to claim 74, characterized in that the amount of activated carbon in the activated carbon element (Q209) is 15% -95% of the volume of the internal cavity of the element.

79. The system for the complete processing of household waste according to claim 1, characterized in that the system also includes an apparatus for producing a hybrid charged adsorbent for processing the remaining solid sludge, while the sludge at the outlet of various sections enters the apparatus for producing a hybrid charged adsorbent.

80. The system for the complete processing of household waste according to claim 1, characterized in that the system also includes a tail gas treatment unit for environmental protection, centralizing the processing of flue gas, hot flue gas, dust and similar products in various processes.

81. The system for the complete processing of household waste according to claim 80, characterized in that the tail gas treatment apparatus for environmental protection includes a tail gas buffer device, a separator for separating gas, water and solids (S257), a rotary spray system with two columns (S259) and a device for separating flue gas (S264), an air buffer (S247) and a pipeline for primary processing of flue gas (S253), tail gas enters the air buffer (S247), enters a pipeline for primary processing of flue gas behind (S253) through the air buffer (S247) and is discharged into the separator for separating gas, water and solids (S257) through the pipeline for primary processing of flue gas (S253), the outlet of the separator for separating gas, water and solids (S257) leads to a rotating spray system with two columns (S259), while the tail gas enters the flue gas recovery device (S264) after processing with a rotating spray system with two columns (S259) and then is output after processing using the device for highlighted I flue gas (S264).

82. A system for the complete processing of household waste according to claim 81, characterized in that the air buffer (S247) includes a cylindrical body, several openings for creating a water curtain (S272) are located in the upper part of the body, and an outlet for sewage is located in the lower part of the body waters (S249).

83. A system for the complete processing of household waste according to claim 81, characterized in that there are several tail gas inlet openings around the body of the tail gas buffer device (S253).

84. A system for the complete processing of household waste according to claim 82, characterized in that the tail gas buffer device also includes a water storage tank, wherein the water outlet (S249) is connected to the water storage tank by a pipe.

85. A system for the complete processing of household waste according to claim 84, characterized in that the pipelines for circulating water are connected to the upper part of the water storage tank using a water valve (S250), the middle and lower parts of the water storage tank are connected to the spray gun to create a water curtain in an air buffer (S247) using pumps and pipelines.

86. System for the complete processing of household waste according to paragraphs. 82-85, characterized in that in the upper part inside the air buffer (S247) also has a liquid level sensor (S251) for detecting the liquid level inside the air buffer (S247).

87. System for the complete processing of household waste according to paragraphs. 81-85, characterized in that there are several emitting negatively charged ceramic elements (S254) located inside the pipeline for primary processing of flue gas (S253), ceramic elements can emit negatively charged ions naturally without a power source, behind each negatively charged ceramic element (S254 ) a high-speed atomizer is installed (S255).

88. A system for the complete processing of household waste according to claim 87, characterized in that a bypass plate (S256) is installed behind the high-speed atomizer (S255).

89. The system for the complete processing of household waste according to claim 88, characterized in that the outlet plate (S256) is an outlet plate obtuse.

90. The system for the complete processing of household waste according to claim 87, characterized in that the negatively charged ceramic elements (S254) are installed on the left, right and upper surfaces of the pipeline for primary processing of flue gas (S253).

91. System for the complete processing of household waste according to paragraphs. 81-85, characterized in that the tail gas processing system also includes a cooling column (S269), a cooling column (S269) cools hot water in a heat exchanger (S266) in the flue gas recovery device (S264).

92. The system for the complete processing of household waste according to claim 1, characterized in that the system also includes an apparatus for plasma photocatalytic deodorization and sterilization of air using negatively charged ions, which processes air with unpleasant odors obtained at various stages of production, as well as air in production areas, while the air intakes of the apparatus for plasma photocatalytic deodorization and air sterilization using negatively charged ions are located around the cing containers with household waste.

93. The system for the complete processing of household waste according to claim 92, characterized in that the apparatus for plasma photocatalytic deodorization and air sterilization using negatively charged ions includes an air supply pipe (T272), a main photocatalytic installation (T274) and an air filter with activated coal (T281), while gas enters the air supply pipe (T272), an anion apparatus is located inside the air supply pipe (T272), gas enters the main photocatalytic installation (T274) through the pipe water supply (T272), inside the main photocatalytic installation (T274) there is an air channel, several ultraviolet lamps (T276) are installed inside the air channel, the emission wavelength of which is from 253 nm to 258 nm, in the rear parts of ultraviolet lamps (T276) photocatalytic plates made of titanium dioxide (T278) are rigidly fixed, the end of the air channel is connected to an activated carbon air filter (T281), gas is discharged through an activated carbon air filter (T281).

94. A system for the complete processing of household waste according to Claim 93, characterized in that the air exhaust pipe (T279) is located between the main photocatalytic installation (T274) and the activated carbon air filter (T281), inside the air exhaust pipe (T279) an anion apparatus is located, the end of the air channel is connected to the air exhaust pipe (T279), the air discharge pipe (T279) is connected to the activated carbon air filter (T281).

95. System for the complete processing of household waste according to claim 93, characterized in that the anion apparatus is an anionic corrugated plate (T273), the anionic corrugated plate (T273) is installed in the form of a stack.

96. System for the complete processing of household waste according to claim 95, characterized in that the anionic corrugated plate (T273) has two sections, the front section is horizontal, the rear section is vertical.

97. System for the complete processing of household waste according to any one of paragraphs. 93-96, characterized in that in the front of the air supply pipe (T272) there is an air supply opening (T270), an automatic shutter valve (T271) is installed in the lower part of the air supply opening (T270).

98. System for the complete processing of household waste according to any one of paragraphs. 93-96, characterized in that on the reverse sides of the ultraviolet lamps (T276) there are smooth reflective plates (T277).

99. System for the complete processing of household waste according to any one of paragraphs. 93-96, characterized in that the air channel in the main photocatalytic installation (T274) is Z-shaped, the plasma generator is located in the corner of the Z-shaped air channel.

100. System for the complete processing of household waste according to any one of paragraphs. 93-96, characterized in that the size and shape of the photocatalytic plates of titanium dioxide (T278) coincide with the cross section of the air channel, while the photocatalytic plates of titanium dioxide can be fixed in the air channel.

101. System for the complete processing of household waste according to any one of paragraphs. 93-96, characterized in that the photocatalytic plates of titanium dioxide (T278) are installed in the form of bee honeycombs.

102. The system for the complete processing of household waste according to claim 101, characterized in that the photocatalytic plates of titanium dioxide (T278) have a thickness of 1 cm to 10 cm and there are several holes in them.

103. Method for the production of processed products based on the use of the system for the complete processing of household waste according to any one of paragraphs. 1-102, including:

A. The collection of household waste and the placement of household waste in an apparatus for cutting waste packages;

B. general screening of household waste after cutting the packages of household waste using an apparatus for general screening of household waste to separate hard plastics and other waste;

C. inactivation of the remaining household waste from which hard plastics were removed using an apparatus for liquid oxidation, deodorization, inactivation, purification and reduction of salt content;

D. dehydration of inactivated waste using a vertical apparatus for dehydration; and

E. Grinding dehydrated material with a grinder.

104. The method according to p. 103, characterized in that the material crushed in step E is subjected to biochemical processing using a biochemical processing apparatus and then dried using an automatic unloading multi-stage drying apparatus for mixed nutrient media after multi-stage drying and sorting of the material.

105. The method according to p. 104, characterized in that the biochemical treatment includes:

A. obtaining pre-fermented material while using an anaerobic fermentation tank (I65) and two secondary fermenters (I71);

B. after completion of the preliminary fermentation step, the material in two secondary fermenters (I71) enters the primary fermenter using an automatic loading device (I74) located in the lower part of the secondary fermenters (I71), while the raw materials in the anaerobic fermentation tank (I65) enter primary fermenter using an automatic loading system (I67) for secondary fermentation; and

C. Unloading material after completion of secondary fermentation.

106. The method according to p. 105, characterized in that upon receipt in the anaerobic fermentation tank (I65) of the material subjected to preliminary fermentation, legume crops, which accounts for 50% -80% of the total weight of the fermentation material, and annual cereal straw, which is 20% -50% of the total weight of the fermentation starting material crumbles into powder with a particle size of 0.5 mm to 1 mm; for the biochemical treatment of the mixed material, a compound inoculant is added, capable of destroying an unprocessed fiber containing at least two ammov, one of which is an Aspergillus oryzae, the starting amount of the composite was 1% inoculum hybrid solid starting material, the chemical composition is added based on calcium oxide, sodium chloride, dibasic sodium phosphate and urea.

107. The method according to p. 106, characterized in that when receiving pre-fermented material in one of the secondary fermenters (I71), artificially inactivated household waste is added to the secondary fermenter (I71) as a starting material, with bran being 1 % -2% of the weight of the starting material, rice, which is 1% -3% of the weight of the starting material, and white sugar, which is 1% of the weight of the starting material, in the form of a mixture, while adding a suitable amount of water to obtain a paste from the mixture and the temperature is controlled in the range from 20 ° C to 30 ° C, baking yeast, which is 2% -4% of the total weight of the mixture, is added, and then completely mixed with the mixture to enhance aeration to stimulate the growth of yeast, while the type of fermentation can represent fermentation.

108. The method according to p. 107, characterized in that when receiving pre-fermented material in one of the secondary fermenters (I71), artificially inactivated, purified and dehydrated household waste is added to the secondary fermenter (I71) as a starting material for the fermentation of solid waste, in this case, strains of Trichoderma viride, Candida tropicalis, aquatic bacteria and Endomycopsis yeast are selected for the formation of a mixed inoculant based on four strains, the weight ratio of four strains is 2: 2: 1: 1, the number of inoculans and makes up 2% of the total weight, at the same time add urea, which is 1% -1.5% of the total weight, the temperature is 25 ° C-42 ° C, the stirrer (I73) stirs the mixture once every hour, fermentation time is from 9 hours to 10 hours.

109. The method according to p. 108, characterized in that during the secondary fermentation, the material subjected to preliminary biochemical treatment enters the primary fermenter, while the fermentation material using straw corresponds to 10% -40% of the total weight of the material, the fermentation material using baking yeast corresponds to 20% of the total weight of the material, the fermentation material in the second secondary fermenter (I71) corresponds to 40% -70% of the total weight of the material, while when three materials after the preliminary fermentation the treatments enter the primary fermenter and the double-layer screw stirrer (I78) rotates 360 degrees to slowly mix materials at low speed, the temperature in the primary fermenter begins to increase from the initial 20 ° C, the average temperature of the materials at the temperature increase stage is 20 ° C-28 ° C, the I87 air valve closes after 4 hours, at the same time the temperature rises to 35 ° C-38 ° C, after 3 hours the I92 air supply unit opens in the first stage to provide little ventilation, It follows that the temperature rises to 82 ° C, after 2 chasa opens I92 apparatus for supplying air to the second stage to ensure strong ventilation.

110. The method according to p. 103, characterized in that the plastic waste obtained in stage B is converted into biodiesel using an apparatus for processing plastic waste.

111. The method according to p. 110, characterized in that the apparatus for artificial aging of the residue and the untreated carbon black obtained in the production of biodiesel fuel is subjected to aging with ozone, while the untreated carbon black after chemical aging enters the apparatus for physical aging, after artificial aging, untreated carbon black enters the device for sorting materials using a special automatic conveyor device, while a quantitative loading device for liquids and solids adds every suitable adjuvant, the materials are completely mixed and, using a multi-layer push-pull threaded rod, are fed into the apparatus for producing low-sulfur environmentally friendly pure coal with a high energy content, and after receiving the materials receive untreated carbon black .

112. The method according to any one of paragraphs. 103-111, characterized in that the wastewater obtained in stages A-E, are recycled or recycled after processing using the apparatus for the rapid treatment of wastewater.

113. The method according to any one of paragraphs. 103-111, characterized in that the solid precipitate obtained in stages A-E, allows you to get a hybrid charged adsorbent after processing using the apparatus for the production of hybrid charged adsorbent.

114. The method according to any one of paragraphs. 103-111, characterized in that the flue gas, hot flue gas, dust and air after applying the pump and drainage obtained in stages A-E are recycled after processing using a processing apparatus to protect the environment.

115. The method according to p. 114, characterized in that after processing the gas is utilized using an apparatus for plasma photocatalytic deodorization and air sterilization using negatively charged ions.

116. The method according to any one of paragraphs. 103-111, characterized in that the mixture of oil and water obtained in stage A-E, allows you to get biodiesel using the method of production of biodiesel without distillation, the method includes:

(1) carrying out the removal of solids from a mixture of oil, water and solids obtained from household waste, using a horizontal device with a screw tape to separate solids and liquids (O151) to obtain a mixture of oil and water;

(2) feeding a mixture of oil and water into an oil and water separation column (O152) for separating oil and water and feeding the separated thick fractions of oil to an oil storage container (O149);

(3) if it is necessary to process lipid substances after the lipid substances are fed into the homogenizer (O158) using devices such as a pump, starting a hydraulic pusher in the form of a propeller (O160), adding phosphoric acid, while the ratio of phosphoric acid to lipid substances does not exceed 0.8% -1.2% of the total amount of oil, the use of a screw in the form of a propeller at the two ends of the homogenizer (O158) to whip the liquids inside the homogenizer (O158), the whipping time is from 10 to 15 minutes, after the end of whipping the liquids immediately add a saline solution as a diluent, the ratio of water to salt in the saline solution is from 95: 5 to 90:10, the ratio of the weight of lipid substances to the saline solution is from 90:10 to 80:20;

(4) continuous operation of the hydraulic pusher in the form of a propeller (O160) for 10 to 20 minutes;

(5) leaving the mixture of thick oil fractions in a homogenizer (O158) for 60 minutes to 120 minutes;

(6) the entry of lipid substances from which the colloid was removed into the exchange device (O161) for thick oil fractions operating at room temperature;

(7) when the level of the thick oil fractions entering the exchange device (O161) for the thick oil fractions operating at room temperature reaches the set liquid level, the flow stops, and the blower pipe (O171) at the bottom of the exchange device starts working (O161 ) for thick fractions of oil operating at room temperature, a loading opening (O169) opens, a solid catalyst and methanol are added, while the amount of solid catalyst is 1.5% -3.5% of the mass of lipid substances, and your methanol is 3% -8% of the mass of lipid substances, and after adding methanol add a co-solvent;

(8) prolonged stirring for 10 minutes to 15 minutes using a stirrer and adding a solid alkaline metal-based catalyst, wherein its amount is 3% -4.5% by weight of lipid substances;

(9) after adding the necessary adjuvant, the loading hole (O169) is closed, the pump for material circulation is started and the ultrasonic generator (O162) is turned on, the initial frequency of the ultrasonic generator (O162) is 25 kHz, the operating time is 1 minute, then the initial frequency gradually increases to 30 kHz, time is from 30 minutes to 40 minutes, the reaction temperature is 25 ° C-35 ° C;

(10) after completion of the exchange of thick fractions in the exchange device (O161) for thick oil fractions operating at room temperature, the mixture of lipid substances is fed to a liquid separation device (O172) for settling and separation, the top layer being a liquid mixture methanol and glycerol, the bottom layer is crude biodiesel; and

(11) opening a liquid separation device in the region of the lower liquid outlet, supplying the crude biodiesel to the filter device (O173), obtaining purified biodiesel after filtration, and recycling the solid catalyst.

117. The method according to p. 116, characterized in that when the oil and water are separated, the oil and water mixture in the oil and water separation column (O152) is heated to 60 ° C-85 ° C, after the rise of lipid substances, the dissociation of oil and water is achieved while the lipid substances in the upper layer are collected using an oil scraper (O155) and sent to the oil storage container through the oil outlet pipe (O156).

118. The method according to p. 116, characterized in that the selected co-solvent is methanol and ethanol in any proportion, the added amount of co-solvent is 0.5% -2% by weight of lipid substances, the co-solvent also includes butanol in an amount of 0.5% by weight of lipid substances.

119. The method according to p. 116, characterized in that the solid metal anionic alkaline catalyst is characterized by the use of reagent-activated carbon and nanoparticles of silicate minerals with a cyclic structure based on aluminum, sodium, iron and lithium as a core with a shell of skeletal media lattice based on silicon, aluminum and lithium, and the presence of charged hybrid carrier having a polarity, the carrier is immersed in a KNO ₃ as a liquid and becomes a solid anionic charged hybrid alkaline catalysis metal-based torus having polarity and contain 15% -25% KNO _3.

120. The method according to p. 116, wherein the biodiesel is converted into emulsified biodiesel using an apparatus for producing microemulsified biodiesel, the method comprising:

(1) supplying the crude biodiesel to the microemulsified biodiesel production apparatus, starting the stirring system, adding 30% -80% of diesel fuel complying with the III National Standard, and then stirring the mixture for 5 minutes;

(2) adding a hydrophilic agent, whose added amount is 2-3% of the total weight of pure biodiesel and diesel fuel corresponding to the III National Standard, and stirring the mixture for 1 minute to 15 minutes;

(3) adding butanol as an intermediate, whose added amount is 2-4% of the total weight of pure biodiesel and biodiesel in accordance with the National Standard III, and continuously mixing the mixture directly for 15 minutes while stirring with a vertical stirrer (P175 ) stirs the mixture at a speed of 100 rpm to 130 rpm;

(4) adding isopentane as a spontaneous combustion temperature regulator, whose added amount is 1.5-2% of the total weight of the purified biodiesel; and

(5) adding oxygen-enriched water, wherein water is 1% -20% of the total weight of the product, stirring the mixture for 15 minutes, adjusting the rotation speed in the range from 170 rpm to 200 rpm and adding cis-9-octadecene acid as an emulsifier, while the added amount of cis-9-octadecenoic acid is 70% -90% of the weight of pure water added, while the mixture is continuously stirred with a mixer until the mixture becomes transparent, after which the rotation speed of the mixer is increased to 280-340 rpm, while the mixture Qdim interfere continuously for 40-60 minutes while after standing for a certain period of time and to achieve transparency and the absence of the emulsified fuel obtained delamination finished product.

121. The method according to p. 120, characterized in that as a hydrophilic agent, a compound based on a cationic surfactant and a nonionic surfactant is used as a composite surfactant, wherein the proportion of cationic surfactant is 50% and the proportion of non-ionic surfactant is 50%.

122. The method according to p. 120, wherein the surfactant is triethanolamine, or hexahydroaniline, or cetrimonium bromide and ammonia.

123. The method according to p. 120, characterized in that the added amount of oxygen-enriched water is 10% -20% of the total weight.

124. The method according to p. 120, characterized in that the acid number of the added cis-9-octadecenoic acid is 200.