CN210261524U - Environment-friendly fatlute pyrolysis equipment - Google Patents

Abstract

The utility model discloses an environment-friendly fatlute pyrolysis equipment uses fatlute pyrolysis utilization technical field, has solved traditional pyrolysis equipment and has used circulating fluidized bed to mix burning coal and pyrolysis sediment and provide the energy for the pyrolysis, contains heavy metal in the pyrolysis sediment, easily brings secondary pollution's technical problem, and its technical scheme main points are: comprises a pyrolysis system, a heat source component and a condensing chamber; the pyrolysis system comprises a heating assembly and a crushing assembly for crushing and breaking up oil sludge; the heat source component comprises a gas storage tank for storing gas and a burner, the burner is communicated with a heat exchanger, a washing cavity and an adsorption cavity are arranged in the condensing chamber, and adsorption filler is filled in the adsorption cavity; the heat exchanger has the technical effects that the heat generated by the combustor is exchanged through the heat exchanger, so that the contact of oil sludge and open fire is avoided, and secondary pollutants such as dioxin and the like are avoided; the adsorption filler adsorbs non-condensable gas and harmful gas, and finally discharged waste gas is prevented from polluting the atmosphere.

Description

Environment-friendly fatlute pyrolysis equipment

Technical Field

The utility model relates to a fatlute pyrolysis utilization technical field, in particular to environment-friendly fatlute pyrolysis equipment.

Background

In the process of petroleum exploitation, transportation and processing in the petrochemical industry, a large amount of oil sludge is generated. According to data, the annual output of oil sludge generated in the process of only extracting oil in China is over million tons. These sludges are difficult to settle and contain large amounts of metal contaminants that, if discharged directly, can contaminate land and water resources. With the overall improvement of the environmental awareness of China and increasingly healthy environmental regulations of China, the treatment technology of oil sludge becomes a hotspot problem in the research of the fields of energy and environmental science at present.

At present, the treatment technology of domestic and foreign oily sludge is mainly classified into 3 types: physical-chemical extraction, biodegradation and heat treatment. The heat treatment method has great advantages in the aspects of harmlessness, reduction and recycling compared with other methods, the main means is incineration and pyrolysis, but the incineration has the problems of large energy consumption, high cost, serious secondary pollution and the like, the pyrolysis has the advantages of no secondary pollution, oil quality improvement, heavy metal stabilization and the like, and recycling and energy recycling are realized.

The existing pyrolysis equipment is heated by adopting steam or an electric furnace, and the energy consumption is higher. Chinese patent 201110082159.9 discloses an integrated method and system for oil sludge pyrolysis regeneration fuel oil, which comprises an oil sludge pyrolysis regeneration fuel oil system and a circulating fluidized bed incineration system; the circulating fluidized bed is used for mixing the burning coal and the pyrolysis slag to provide energy for pyrolysis, and the pyrolysis slag contains heavy metals and is easy to cause secondary pollution. It is desirable to provide a pyrolysis apparatus with reduced pollutant emissions and environmental protection.

SUMMERY OF THE UTILITY MODEL

The utility model aims at providing an environment-friendly oil sludge pyrolysis device, which has the advantages that the heat generated by a burner is exchanged through a heat exchanger, and the contact of oil sludge and open fire is avoided, so that the generation of secondary pollutants such as dioxin and the like is avoided; the adsorption filler in the adsorption cavity adsorbs the non-condensable gas and the harmful gas, so that the finally discharged waste gas is prevented from polluting the atmosphere.

The above technical purpose of the present invention can be achieved by the following technical solutions: an environment-friendly oil sludge pyrolysis device comprises a pyrolysis system for pyrolyzing oil sludge, a heat source assembly for supplying heat to the pyrolysis system and a condensation chamber;

the pyrolysis system comprises a heating assembly for heating oil sludge and a crushing assembly for crushing and scattering the oil sludge, the heating assembly comprises a shell and an interlayer shell arranged outside the shell, a heating cavity is formed between the interlayer shell and the shell, a hot air inlet and a cold air outlet are formed in the interlayer shell, the hot air inlet and the cold air outlet are communicated with the heating cavity, a feeding hole and a discharging hole are formed in the shell, and a gas phase discharging pipe is arranged on the shell;

an evaporation cavity is arranged on the shell, and an integrated temperature transmitter for detecting the temperature in the evaporation cavity is arranged on the shell;

the heat source assembly comprises a gas storage tank and a burner, wherein the gas storage tank is used for storing gas, and the gas storage tank is communicated with the burner; the combustor is provided with a hot air outlet, the combustor is communicated with a heat exchanger, the heat exchanger is provided with a heat medium outlet and a heat medium inlet, the hot air outlet is communicated with the heat medium inlet, and the heat medium outlet is communicated with the hot air inlet;

a condensation inlet is arranged on the condensation chamber, the condensation inlet is communicated with the gas phase discharge pipe, and a washing cavity and an adsorption cavity are sequentially arranged in the condensation chamber along the direction far away from the condensation inlet; the washing chamber is internally provided with a condensation washing component for condensing oil and water in a gas phase, the absorption chamber is filled with an absorption filler, and one side of the condensation chamber, which is far away from the condensation inlet, is provided with a waste gas outlet.

Through above-mentioned technical scheme, feed inlet on the casing is arranged in supplying fatlute to enter into the casing, and the discharge gate on the casing is used for supplying to be extracted the mud discharge after crude oil is passed, and the casing is used for temporarily holding fatlute, and the heating chamber is used for the medium after the storage heating to fatlute can be quick by the heating, thereby make crude oil and moisture in the fatlute can be quick evaporate into gaseous state. The burner is used for burning the fuel in the air storage tank so as to obtain heat energy; the heat exchanger is used for transferring heat energy generated in the heat source assembly to the medium in the heat exchanger, so that the medium can bring the heat energy into the heating cavity, the combustion of fuel is separated from the heating cavity in the pyrolysis system, the direct contact of the shell with open fire is avoided, the possibility of combustion of crude oil in the shell is avoided, crude oil can be obtained as much as possible, and secondary pollution caused by crude oil combustion is avoided. The evaporation cavity is used for buffering oil and water in a gas phase, the shell is prevented from being damaged due to overlarge pressure, and the integrated temperature transmitter is used for monitoring the temperature in the evaporation cavity so as to control the temperature in the most appropriate range, so that less fuel is adopted to keep continuous pyrolysis of the oil sludge. The condensation washing component in the washing cavity is used for washing and condensing the oil and water in the gas phase, so that the oil and water in the gas phase are quickly converted into an oil-water mixture in the liquid phase; the adsorption filler in the adsorption cavity is used for adsorbing non-condensable gas and toxic and harmful gas, thereby ensuring that the gas discharged into the air does not pollute the atmosphere.

The utility model discloses further set up to: the condensation washing assembly comprises a spray head and a pall ring, the spray head is arranged at the top of the washing cavity, and the pall ring is filled in the washing cavity; the bottom of the condensing chamber is a liquid leakage pore plate, a storage box used for storing an oil-water mixture is arranged below the condensing chamber, and the spray header is communicated with a water storage tank.

Through the technical scheme, the spray header is used for spraying water at normal temperature, so that oil and water in gas phase can be rapidly condensed when entering the washing cavity, and the pall ring is used for shunting liquid and gas, so that oil-water mixture in liquid phase can be rapidly converged together; the leakage orifice plate is used for allowing the liquid-phase oil-water mixture to pass through, and the storage tank is used for storing the liquid-phase oil-water mixture, so that the oil-water mixture can be well settled.

The utility model discloses further set up to: the gas storage tank stores liquefied gas.

By the technical scheme, the liquefied gas is cheap, and the toxic and harmful substances generated by combustion are few, so that the liquefied gas is a cleaner fuel; therefore, the combustor can obtain more heat energy when combusting the liquefied gas, and cannot pollute the environment.

The utility model discloses further set up to: the upper portion of storage tank is equipped with the second liquid phase export, the second liquid phase export intercommunication has oil water separating equipment, oil water separating equipment is last to be equipped with crude oil export and waste water outlet, waste water outlet and tank intercommunication.

Through above-mentioned technical scheme, the waste water that obtains after subsiding can let in the tank to recycle, the better water economy resource has improved the utilization ratio of water.

The utility model discloses further set up to: the cold air outlet is communicated with a hot air circulating fan, the hot air circulating fan is provided with an air outlet pipe, the heat exchanger is provided with a refrigerant inlet, and the air outlet pipe is communicated with the refrigerant inlet.

Through the technical scheme, the heat generated by the burner is recycled through the hot air circulating fan, so that the utilization rate of heat energy is improved, the fuel consumption is well saved, the economic cost is saved, and the emission of waste gas is also reduced.

The utility model discloses further set up to: the casing is connected with the driving shaft in the rotation, be equipped with first paddle on the driving shaft, first paddle is equipped with a plurality ofly along the axis direction of driving shaft, and is a plurality of first paddle is the heliciform and is interrupted the setting.

According to the technical scheme, the first paddle is arranged in a spiral discontinuous mode, so that the first paddle can cut and crush the oil sludge, the oil sludge can absorb heat more sufficiently, and the utilization rate of the heat is improved; and the oil sludge is continuously pushed forward, so that the oil sludge can be subjected to continuous pyrolysis processing, and the pyrolysis efficiency of the oil sludge is improved.

The utility model discloses further set up to: the shell is rotatably connected with a driven shaft, a driving gear is arranged on the driving shaft, and a driven gear meshed with the driving gear is arranged on the driven shaft; the driven shaft is provided with a plurality of second paddles, the second paddles are arranged in a plurality of positions along the axis direction of the driven shaft, the second paddles are arranged in a spiral shape in an interrupted mode, and the first paddles and the second paddles are arranged in a staggered mode.

Through the technical scheme, the driven shaft and the driving shaft can synchronously rotate due to the meshing of the driving gear and the driven gear, so that the first paddle and the second paddle can repeatedly cut and crush the oil sludge, the oil sludge is crushed into small particles, and the heat absorption rate of the oil sludge is improved; because the spiral of first paddle and second paddle is to opposite, in addition driving gear and driven gear meshing to make first paddle and second paddle can impel fatlute to move towards same direction simultaneously in the cutting process to fatlute, make the efficiency of the breakage and the transmission of fatlute higher, further improvement the efficiency of fatlute pyrolysis.

The utility model discloses further set up to: the oil sludge washing device is characterized in that the feed port is communicated with an oil sludge washing tank for adding an oil sludge washing dispersant, an extension stirring shaft is rotatably connected in the oil sludge washing tank, and an oil sludge stirring blade is connected to the extension stirring shaft.

Through above-mentioned technical scheme, stirring vane rotates and makes fatlute and fatlute washing dispersant mix more even to make oil and the hydroenergy in the fatlute can be better emulsified, thereby make the mobility of oil and water better, make oil and water be more easily extracted.

The utility model discloses further set up to: the outer side of the interlayer shell is coated with a heat-insulating layer.

Through above-mentioned technical scheme, the heat preservation is used for isolated thermal conduction, has avoided the heat to scatter and disappear out from the heating chamber to make the heat in the heating chamber can be abundant utilized, make fatlute absorption heat that can be more abundant, further improvement when fatlute pyrolysis to thermal utilization ratio.

The utility model discloses further set up to: be equipped with the water conservancy diversion piece in the heating chamber, the water conservancy diversion piece is equipped with a plurality ofly, and is a plurality of along the length direction of casing the both sides of water conservancy diversion piece are laminated in casing and intermediate layer shell respectively, be equipped with hot-blast hole between the one end of water conservancy diversion piece and the casing, two adjacent hot-blast hole on the water conservancy diversion piece is crisscross to be set up.

Through above-mentioned technical scheme, the water conservancy diversion piece is arranged in the hot-blast flow of guide heating chamber for hot-blast abundant and the casing contact, thereby make the fatlute in the casing can be abundant the heat in the hot-blast absorption, and then better improvement fatlute pyrolysis to thermal utilization ratio.

To sum up, the utility model discloses following beneficial effect has:

1. the heat exchanger is used for transferring the heat energy generated in the heat source assembly to the medium in the heat exchanger, so that the medium can bring the heat energy into the heating cavity, the shell is prevented from directly contacting open fire, the possibility of burning crude oil is avoided, more crude oil can be obtained, and secondary pollution caused by burning crude oil is avoided;

2. the adsorption filler in the adsorption cavity is used for adsorbing non-condensable gas and toxic and harmful gas, thereby ensuring that the gas discharged into the air does not pollute the atmosphere.

Drawings

Fig. 1 is an overall configuration diagram of the present embodiment;

fig. 2 is a schematic structural diagram of the sludge preliminary separation system according to the present embodiment;

FIG. 3 is a schematic structural view of a heat source module and a thermal cycle module of the present embodiment;

FIG. 4 is a schematic structural view of the pyrolysis system of the present embodiment;

FIG. 5 is a schematic structural view of the nitrogen shield assembly of the present embodiment;

FIG. 6 is a schematic view of the internal structure of the pyrolysis system of the present embodiment;

FIG. 7 is a schematic structural view of the transmission assembly and the crushing assembly of the present embodiment;

FIG. 8 is an enlarged schematic view of portion A of FIG. 6;

FIG. 9 is a schematic view showing the positional relationship of the gas phase discharge pipe and the housing of the present embodiment;

FIG. 10 is an enlarged schematic view of portion B of FIG. 5;

fig. 11 is a schematic structural view of the condensing system of the present embodiment.

Reference numerals: 1. an oil-sludge preliminary separation system; 2. a pyrolysis system; 3. a heating system; 4. an explosion-proof system; 5. a condensing system; 7. a sludge washing assembly; 8. a horizontal screw centrifuge; 9. an oil sludge washing pool; 10. an oil sludge stirring blade; 11. a high temperature steam generator; 12. a first sludge outlet; 13. a first liquid phase outlet; 14. a first solid phase outlet; 15. a heating assembly; 16. a crushing assembly; 17. a transmission assembly; 18. a housing; 19. a heating cavity; 20. a hot air inlet; 21. a cold air outlet; 22. a heat-insulating layer; 23. a drive shaft; 24. a driven shaft; 25. an installation section; 26. a first blade; 27. a sandwich housing; 28. a heat source assembly; 29. a thermal cycle assembly; 30. a gas storage tank; 31. a burner; 32. a hot air outlet; 33. a hot air circulating fan; 34. an air outlet pipe; 35. a return air duct; 36. a heat exchanger; 37. a heating medium inlet; 38. a refrigerant inlet; 39. a heating medium outlet; 40. a first exhaust gas outlet; 41. a feed inlet; 42. a discharge port; 43. a hot air pipe; 44. a hot air branch pipe; 45. a drive motor; 46. a driving gear; 47. a driven gear; 48. mounting a plate; 49. a speed reducer; 51. a cooling assembly; 52. a nitrogen protection component; 53. an input end bearing seat; 54. a tail end bearing seat; 55. a water storage sleeve; 56. a water inlet hole; 57. a water outlet hole; 59. a cooling water pipe; 60. a cooling water pump; 61. a nitrogen storage tank; 62. a nitrogen shaft seal ring; 63. a negative pressure pipeline; 64. an electromagnetic valve; 65. an oxygen concentration sensor; 66. an air inlet pipe; 67. a gas delivery pipe; 68. a sampling tube; 69. an integrated temperature transmitter; 70. an evaporation chamber; 71. a gas phase discharge pipe; 72. a discharge pipe mounting plate; 73. a condensation inlet; 74. a second exhaust gas outlet; 75. a high pressure fan; 76. a washing chamber; 77. a drying chamber; 78. an adsorption chamber; 79. a shower head; 80. pall ring; 81. a water storage tank; 82. a high pressure water pump; 83. a condensing chamber; 84. a condensing and washing assembly; 85. a storage box; 86. drying the filler; 87. an oil-water separation device; 88. a liquid phase inlet; 89. a crude oil outlet; 90. a waste water outlet; 91. a second liquid phase outlet; 92. a stirring motor; 93. the stirring shaft is prolonged; 94. a flow deflector; 95. a hot air through hole; 96. maintaining the cover plate; 97. maintaining the window; 98. installing a flanging; 99. a sealing groove; 100. sealing the inserting plate; 101. a heat preservation box; 102. a heat preservation cavity; 103. a second blade.

Detailed Description

The present invention will be described in further detail with reference to the accompanying drawings.

Example (b):

referring to fig. 1, an environment-friendly oil sludge pyrolysis apparatus includes an oil sludge preliminary separation system 1, a pyrolysis system 2, a heat supply system 3, an explosion-proof system 4, a condensation system 5, and an oil-water separation apparatus 87; the oil sludge preliminary separation system 1 is used for carrying out preliminary treatment on oil sludge containing more liquid phases and separating out a part of liquid phases which are well separated from the oil sludge; the pyrolysis system 2 is used for fully pyrolyzing the oil sludge, so that water, oil and solid phases in the oil sludge are separated, and the purpose of fully pyrolyzing the oil sludge is achieved; the heat supply system 3 is used for supplying heat to the pyrolysis system 2, so that the oil sludge in the pyrolysis system 2 can be kept at a temperature of about 500 ℃, and crude oil and water in the oil sludge can be decomposed in a gas phase; the explosion-proof system 4 is used for filling nitrogen into the pyrolysis system 2, and reducing the oxygen content in the pyrolysis system 2 to below 1%, so that the crude oil has no combustion or explosion condition, thereby avoiding the combustion or explosion of the crude oil and ensuring the pyrolysis safety of the oil sludge; the condensing system 5 is used for condensing and settling out crude oil and moisture in the gas phase so as to recycle the oil and water; the oil-water separating device 87 is used to separate water and oil in a liquid phase for sufficient recovery of the water and oil.

Referring to fig. 2, the sludge preliminary separation system 1 comprises a sludge wash module 7 for emulsifying oil and water in the sludge and a decanter centrifuge 8 for preliminarily separating solid and liquid phases; the sludge washing assembly 7 comprises a sludge washing pool 9, a sludge stirring blade 10 rotatably arranged on the sludge washing pool 9 and a high-temperature steam generator 11 communicated with the sludge washing pool 9. The oil sludge washing pool 9 is used for containing oil sludge, and a first oil sludge outlet 12 is formed in the bottom of the oil sludge washing pool 9; adding an oil sludge washing dispersant into the oil sludge washing pool 9, wherein the oil sludge washing dispersant can adopt mixed alkali consisting of inorganic alkali and inorganic salt, and can also adopt an environment-friendly dispersant for treating oily sludge disclosed in the Chinese invention patent with the publication number of 106277710A; high-temperature steam generated by the high-temperature steam generator 11 is communicated into the oil sludge washing pool 9 through a pipeline, and the high-temperature steam heats a mixture of oil sludge and an oil sludge washing dispersant in the oil sludge washing pool 9, so that oil and water in the oil sludge can be emulsified more quickly; fixedly connected with agitator motor 92 on the fatlute washing pond 9, fixedly connected with extension (mixing) shaft 93 on agitator motor 92's the main shaft, extension (mixing) shaft 93 and fatlute stirring vane 10 fixed connection, agitator motor 92 can drive fatlute stirring vane 10 and stir the fatlute in the fatlute washing pond 9 for fatlute and fatlute wash the more even of dispersant mixture, thereby make oil and the more thorough and high-efficient that can emulsify of hydroenergy in the fatlute.

Referring to fig. 2, the decanter centrifuge 8 is preferably a sludge wastewater treatment centrifuge of model LW420X1800Y, manufactured by shanghai ruiwei electromechanical devices limited, and performs a preliminary centrifugal separation of the solid and liquid phases of the sludge to separate a portion of the oil and water from the sludge; a screw conveyor is arranged between the horizontal screw centrifuge 8 and the oil sludge washing tank 9, and a feed inlet 41 is formed in the horizontal screw centrifuge 8; a first oil sludge outlet 12 of the oil sludge washing pool 9 corresponds to a feed port 41 on the horizontal decanter centrifuge 8, and emulsified oil sludge is conveyed into the horizontal decanter centrifuge 8 from the first oil sludge outlet 12 by a screw conveyor; the horizontal screw centrifuge 8 is provided with a first liquid phase outlet 13 and a first solid phase outlet 14, the first liquid phase outlet 13 is used for discharging oil and water, the first solid phase outlet 14 is used for discharging solid phase, and the discharged solid phase also contains part of oil and water.

Referring to fig. 3, the heating system 3 includes a heat source assembly 28 and a heat circulation assembly 29 for providing heat energy, the heat source assembly 28 includes a gas storage tank 30 for storing liquefied natural gas and a burner 31, a pipeline is provided between the gas storage tank 30 and the burner 31, the pipeline transports the liquefied natural gas in the gas storage tank 30 to the burner 31, a hot air outlet 32 is provided on the burner 31, and the hot air outlet 32 is used for outputting heated gas; the thermal circulation assembly 29 comprises a hot air circulation fan 33 for conveying hot air, an air outlet pipe 34 communicated with the hot air circulation fan 33 and an air return pipe 35 communicated with the hot air circulation fan 33, and the air outlet pipe 34 is communicated with a heat exchanger 36. The heat exchanger 36 is preferably a combined plate heat exchanger, the end of the heat exchanger 36 close to the burner 31 is provided with a heat medium inlet 37 and a refrigerant inlet 38, the end of the heat exchanger 36 far from the refrigerant inlet 38 is provided with a heat medium outlet 39, and the end of the heat exchanger 36 far from the heat medium inlet 37 is provided with a first waste gas outlet 40.

Referring to fig. 4 and 6, the pyrolysis system 2 comprises a heating assembly 15 for heating the sludge, a breaking assembly 16 for breaking up and breaking up the sludge, and a transmission assembly 17; the heating assembly 15 comprises three shells 18 arranged along the vertical direction and a sandwich shell 27 fixedly arranged on the outer side of the shell 18, the sandwich shell 27 and the shell 18 are provided with a heating cavity 19, the cross section of the shell 18 is approximately U-shaped, the shell 18 is cast by nickel series heat-resistant cast iron, and the upper side of the shell 18 is provided with an evaporation cavity 70.

Referring to fig. 5 and 6, the heating cavity 19 is disposed outside the circular arc segment, a plurality of flow deflectors 94 are disposed in the heating cavity 19, the flow deflectors 94 are disposed along the length direction of the casing 18, two sides of the plurality of flow deflectors 94 are respectively attached to the casing 18 and the interlayer housing 27, hot air through holes 95 are disposed between one end of each flow deflector 94 and the casing 18, and the hot air through holes 95 on two adjacent flow deflectors 94 are disposed on two sides of the casing 18 in a staggered manner; be equipped with on the intermediate layer shell 27 all with hot-blast entry 20 and the cold wind export 21 of heating chamber 19 intercommunication, hot-blast entry 20 and cold wind export 21 set up respectively at intermediate layer shell 27 along length direction's both ends, and intermediate layer shell 27's the outside is fixed with heat preservation 22, and heat preservation 22 is preferred: porous ceramics made of aluminosilicate materials. An integrated temperature transmitter 69 is secured to the outside of housing 18, with integrated temperature transmitter 69 preferably being an integrated temperature transmitter 69 model SBWZ-2480/236.

Referring to fig. 6 and 7, a group of crushing assemblies 16 are respectively and correspondingly arranged on three shells 18, each crushing assembly 16 comprises a driving shaft 23 and a driven shaft 24 which are rotatably connected with the shells 18, mounting sections 25 are respectively arranged on the driving shaft 23 and the driven shafts 24, the mounting sections 25 are arranged in the shells 18, the cross sections of the mounting sections 25 are in a cross shape, first blades 26 are mounted on the mounting sections 25 of the driving shafts 23 through bolts, a plurality of first blades 26 are spirally arranged around the axis of the driving shaft 23, and a plurality of second blades 103 are spirally arranged around the axis of the driven shaft 24; the spiral directions of the first blade 26 and the second blade 103 are opposite, the first blade 26 and the second blade 103 are both arranged discontinuously, and four blades are uniformly distributed on one pitch of the first blade 26 and the second blade 103; the first blade 26 and the second blade 103 are staggered.

Referring to fig. 3 and 5, the hot air outlet 32 is in communication with the heating medium inlet 37 through a pipe, and the air outlet pipe 34 is in communication with the cooling medium inlet 38; the hot air pipe 43 is communicated with the hot air outlet 39, the hot air pipe 43 is communicated with three hot air branch pipes 44, and the three hot air branch pipes 44 are respectively communicated with the hot air inlets 20 on the three heating cavities 19; the return air pipe 35 is communicated with three return air branch pipes which are respectively communicated with the cold air outlet 21 on the heating cavity 19. The gas storage tank 30 feeds liquefied natural gas into the burner 31, the burner 31 burns the liquefied natural gas to heat air, then the heated hot gas enters the heat exchanger 36 from the hot air outlet 32, and the heat exchanger 36 transfers heat energy to the air in the hot air pipe 43.

Referring to fig. 3 and 6, the heated air circulating fan 33 pumps heated air into the heating cavity 19, the heat in the heating cavity 19 heats the oil sludge in the casing 18, and the oil sludge is crushed and stirred by the paddle 26, so that the oil sludge can be heated more sufficiently, and the oil and water in the oil sludge can be evaporated into a gas phase more sufficiently and rapidly; the air with heat flows from one end of the hot air inlet 20 to one end of the cold air outlet 21, the heat is absorbed by the oil sludge in the shell 18 and then is changed into air with relatively low heat, and the air with low heat is pumped and discharged into the heat exchanger 36 from the cold air outlet 21 by the hot air circulating fan 33; the circulation is carried out in such a way that the sludge in the shell 18 is kept at a constant high temperature all the time; in the environment of continuous high temperature, water and oil in the sludge in the shell 18 are evaporated into gas phase, so that the water and oil in the sludge are more completely separated.

Referring to fig. 5 and 7, three shells 18 are respectively provided with a feed inlet 41 and a discharge outlet 42, the feed inlet 41 is arranged above the shell 18, the discharge outlet 42 is arranged below the shell 18, and the feed inlet 41 and the discharge outlet 42 are respectively arranged at two ends of the shell 18 along the length direction; the discharge port 42 of the upper shell 18 corresponds to and communicates with the feed port 41 of the middle shell 18, and the discharge port 42 of the middle shell 18 corresponds to and communicates with the feed port 41 of the lower shell 18. The paddle 26 rotates to push the oil sludge from the feed port 41 to the discharge port 42, and the paddle 26 on the driving shaft 23 and the driven shaft 24 crushes and stirs the oil sludge in the pushing process.

Referring to fig. 7, a group of transmission assemblies 17 are respectively and correspondingly arranged on the three housings 18, each transmission assembly 17 includes a driving motor 45, a driving gear 46 and a driven gear 47, the driving gear 46 is connected with the driving shaft 23 through a flat key, the driven gear 47 is connected with the driven shaft 24 through a flat key, the driven gear 47 is engaged with the driving gear 46, and the driving motor 45 is used for driving the driving shaft 23 to rotate; an installation plate 48 is fixed at one end of the shell 18 close to the driving motor 45, the driving motor 45 is fixedly arranged on the installation plate 48, a speed reducer 49 is fixed on the installation plate 48, a main shaft of the driving motor 45 is connected with an input shaft of the speed reducer 49 through a coupler, and an output shaft of the speed reducer 49 is connected with a driving main shaft through a coupler. The driving motor 45 drives the driving shaft 23 to rotate, and the driven gear 47 is meshed with the driving gear 46, so that the driven shaft 24 and the driving shaft 23 rotate in opposite directions; and the rotating directions of the paddles 26 on the driving shaft 23 and the driven shaft 24 are opposite, so that the paddles 26 on the driving shaft 23 and the driven shaft 24 can push the sludge to move in the same direction. Because the paddles 26 are intermittent, the sludge will travel to a stop when moving forward, and when the sludge stops, just the paddle 26 on the other shaft rotates, i.e. the paddle 26 cuts into the sludge mass and continues to push the sludge forward. The oil sludge is cut and pushed continuously by repeating the steps.

Referring to fig. 7 and 8, a plurality of maintenance windows 97 with the same size are formed at the vertical section at the upper side of the shell 18, the maintenance windows 97 are used for workers to observe the inside of the shell 18, the blades 26 are convenient to mount and dismount through the maintenance windows 97, a mounting flange 98 is fixed at the position, located at the maintenance windows 97, of the shell 18, a sealing groove 99 with the section being "Contraband" is fixed around the inner sides of the maintenance windows 97, and sealing filler is filled in the sealing groove 99; the mounting flange 98 is connected with a maintenance cover plate 96 through a bolt, one side of the maintenance cover plate 96 facing the shell 18 is fixedly provided with a sealing insert plate 100, and the sealing insert plate 100 is inserted into a sealing filler in a sealing groove 99, so that the sealing property of the shell 18 is better ensured, and the gas in the evaporation cavity 70 is prevented from leaking out; a heat preservation box 101 is fixed on one side of the maintenance cover plate 96 facing the shell 18, a heat preservation cavity 102 is formed between the heat preservation box 101 and the maintenance cover plate 96, and the heat preservation layer 22 is filled in the heat preservation cavity 102; the maintenance cover plates 96 are arranged in parallel along the length direction of the shell 18, and when a certain section of the blade 26 needs to be maintained, only the corresponding maintenance cover plate 96 needs to be detached, so that the maintenance efficiency is improved.

Referring to fig. 6 and 9, a gas phase discharge pipe 71 is provided at one maintenance window 97 of a plurality of maintenance windows 97, a discharge pipe mounting plate 72 is fixed to the gas phase discharge pipe 71, and the discharge pipe mounting plate 72 is connected to the mounting flange 98 by bolts; the gas phase discharge pipe 71 is arranged on the side of the discharge pipe mounting plate 72 far away from the shell 18, and the caliber of the gas phase discharge pipe 71 is gradually reduced towards the direction far away from the shell 18; the oil and water in the vapor phase in the evaporation chamber 70 are discharged to the outside of the casing 18 through the vapor phase discharge pipe 71.

Referring to fig. 5 and 10, the explosion-proof system 4 comprises a cooling assembly 51 and a nitrogen protection assembly 52, an input end bearing seat 53 is fixed on the mounting plate 48, the input end bearing seats 53 correspond to the driving shaft 23 and the driven shaft 24 one by one, and a tail end bearing seat 54 is fixed at one end of the housing 18 far away from the input end bearing seats 53; bearings are fixed in the input end bearing seat 53 and the tail end bearing seat 54, inner rings of the bearings are fixedly connected with the driving shaft 23 or the driven shaft 24, and sealing rings are arranged between the inner rings of the bearings and outer rings of the bearings; the cooling assembly 51 comprises a water storage sleeve 55, a water inlet hole 56 formed in the water storage sleeve 55, a water outlet hole 57 formed in the water storage sleeve 55 and a water storage tank (not shown in the figure), wherein the water storage sleeve 55 is fixedly connected with the input end bearing seat 53 or the tail end bearing seat 54; the storage water tank is used for saving the cooling water, all is equipped with condenser tube 59 between storage water tank and inlet opening 56 and the apopore 57, is equipped with cooling water pump 60 on the condenser tube 59, and cooling water pump 60 can carry out the pump drainage to water to make the cooling water circulate, better take away the heat on driving shaft 23, driven shaft 24 and the bearing, thereby better avoid the bearing to damage because the high temperature.

Referring to fig. 5 and 10, the nitrogen protection assembly 52 includes a nitrogen storage tank 61, a nitrogen shaft seal ring 62, an electromagnetic valve 64, and an oxygen concentration sensor 65 disposed on the housing 18, the nitrogen storage tank 61 is used for storing compressed nitrogen, both ends of the housing 18 located at the input end bearing seat 53 and the tail end bearing seat 54 are provided with an air inlet pipe 66, the air inlet pipe 66 is communicated with the housing 18, an air inlet pipe 67 is disposed between the nitrogen storage tank 61 and the air inlet pipe 66, and the electromagnetic valve 64 is disposed on the air inlet pipe 67. A sampling tube 68 is fixed on the position of the shell 18 close to the air inlet tube 66, the sampling tube 68 is communicated with the inside of the shell 18, the oxygen concentration sensor 65 is fixed on the sampling tube 68, and a probe of the oxygen concentration sensor 65 is inserted in the sampling tube 68; the two ends of the driving shaft 23 and the driven shaft 24 are sleeved with the nitrogen shaft seal ring 62, the nitrogen shaft seal ring 62 is arranged on the outer side of the shell 18, one end of the nitrogen shaft seal ring 62 is fixedly connected with the input end bearing seat 53 or the tail end bearing seat 54, one end of the nitrogen shaft seal ring 62, which is far away from the input end bearing seat 53 or the tail end bearing seat 54, is connected with the water storage sleeve 55 through a bolt, an air inlet nozzle is fixed on the nitrogen shaft seal ring 62 and is communicated with an inner hole of the nitrogen shaft seal ring 62, and the nitrogen storage tank 61 is communicated with the air inlet nozzle through an air pipe.

Referring to fig. 6 and 11, the condensing system 5 includes a condensing chamber 83, a condensing washing assembly 84, and a storage tank 85 disposed below the condensing chamber 83. The condensing chamber 83 is provided with a condensing inlet 73, one side of the condensing chamber 83, which is far away from the condensing inlet 73, is provided with a second waste gas outlet 74, the bottom of the condensing chamber 83 is a liquid leakage pore plate, the inside of the condensing chamber 83 is divided into a washing cavity 76, a drying cavity 77 and an adsorption cavity 78, and the washing cavity 76, the drying cavity 77 and the adsorption cavity 78 are sequentially arranged from the condensing inlet 73 to the second waste gas outlet 74; the condensation inlet 73 is communicated with the gas phase discharge pipe 71 through a negative pressure pipe 63, a high pressure fan 75 is arranged on the negative pressure pipe 63, the high pressure fan 75 is preferably a high pressure centrifugal fan with model number RB-71D-2 manufactured by the full wind environmental protection technology limited company, and the high pressure fan 75 pumps and discharges the oil and the water in the gas phase from the evaporation cavity 70 to the condensation chamber 83.

Referring to fig. 11, the condensing washing assembly 84 includes a shower head 79 and a pall ring 80, the shower head 79 is fixedly disposed at the top of the washing chamber 76, the shower head 79 is communicated with a water storage tank 81 through a pipeline, and a high pressure water pump 82 is disposed on the pipeline between the shower head 79 and the water storage tank 81; the high pressure water pump 82 sprays the water in the water storage tank 81 from the shower head 79, and the water is sprayed from the shower head 79, so that the sprayed water can be quickly contacted with the oil and water in the gas phase in the washing cavity 76, and the oil and water in the gas phase are quickly cooled and condensed into oil drops and water drops. The pall ring 80 is a packing for gas-liquid separation, and the pall ring 80 is filled in the middle lower portion in the washing chamber 76; after the liquefied water drops and oil drops contact with the pall ring 80 in the washing cavity 76, the liquefied water drops and oil drops are adhered to the surface of the pall ring 80 and separated from air, after the oil drops and the water drops adhered to the pall ring 80 continuously have new oil drops and are in collision contact with each other, the oil drops and the water drops are coarsely granulated, and when the gravity is larger than the adsorption force, the oil drops and the water drops leave the pall ring 80 and fall into the storage tank 85. The oil and water in the storage tank 85 is kept still for a period of time, and the oil and water are primarily separated under the action of gravity.

Referring to fig. 11, the gas enters the drying chamber 77 after passing through the washing chamber 76, and the middle lower part of the drying chamber 77 is uniformly filled with a dry filler 86, wherein the dry filler 86 is preferably a pall ring 80; the gas in the drying chamber 77 contacts with the pall ring 80, water drops and oil drops in the gas are further adsorbed by the pall ring 80, and the moisture and oil in the gas are thoroughly separated; the adsorption cavity 78 is uniformly filled with an adsorption filler, preferably activated carbon, which can adsorb non-condensable gas and other harmful gases, so that the purified gas is discharged from the second waste gas outlet 74.

Referring to fig. 2 and 11, the oil-water separation device 87 is preferably a disk centrifuge with a model of DHC470, a liquid phase inlet 88, a crude oil outlet 89 and a wastewater outlet 90 are formed in the oil-water separation device 87, a second liquid phase outlet 91 is formed in the upper portion of the storage tank 85, and the first liquid phase outlet 13 and the second liquid phase outlet 91 of the horizontal decanter centrifuge 8 are both communicated with the liquid phase inlet 88 through pipelines; the oil-water mixture in the storage tank 85 and the oil-water mixture separated in the horizontal decanter centrifuge 8 enter the oil-water separation device 87 through the liquid phase inlet 88, and then the oil-water separation device 87 further separates the oil-water mixture, so that the separated crude oil is rapidly discharged from the crude oil outlet 89 and the separated waste water is discharged from the waste water outlet 90.

The present embodiment is only for explaining the present invention, and it is not limited to the present invention, and those skilled in the art can make modifications to the present embodiment without inventive contribution as required after reading the present specification, but all of them are protected by patent laws within the scope of the claims of the present invention.

Claims (10)

1. An environment-friendly oil sludge pyrolysis device is characterized by comprising a pyrolysis system (2) for pyrolyzing oil sludge, a heat source component (28) for supplying heat to the pyrolysis system (2), and a condensing chamber (83);

the pyrolysis system (2) comprises a heating assembly (15) for heating oil sludge and a crushing assembly (16) for crushing and scattering the oil sludge, the heating assembly (15) comprises a shell (18) and an interlayer shell (27) arranged on the outer side of the shell (18), a heating cavity (19) is formed by the interlayer shell (27) and the shell (18), a hot air inlet (20) and a cold air outlet (21) are formed in the interlayer shell (27), the hot air inlet (20) and the cold air outlet (21) are both communicated with the heating cavity (19), a feeding hole (41) and a discharging hole (42) are formed in the shell (18), and a gas phase discharge pipe (71) is arranged on the shell (18);

an evaporation cavity (70) is arranged on the shell (18), and an integrated temperature transmitter (69) for detecting the temperature in the evaporation cavity (70) is arranged on the shell (18);

the heat source assembly (28) comprises a gas storage tank (30) used for storing gas and a burner (31), and the gas storage tank (30) is communicated with the burner (31); the hot air outlet (32) is formed in the combustor (31), the heat exchanger (36) is communicated with the combustor (31), a hot air outlet (39) and a hot air inlet (37) are formed in the heat exchanger (36), the hot air outlet (32) is communicated with the hot air inlet (37), and the hot air outlet (39) is communicated with the hot air inlet (20);

a condensation inlet (73) is formed in the condensation chamber (83), the condensation inlet (73) is communicated with the gas phase discharge pipe (71), and a washing cavity (76) and an adsorption cavity (78) are sequentially arranged in the condensation chamber (83) along the direction far away from the condensation inlet (73); the washing chamber (76) is internally provided with a condensation washing component (84) for condensing oil-water in a gas phase, the adsorption chamber (78) is filled with adsorption filler, and one side of the condensation chamber (83) far away from the condensation inlet (73) is provided with a second waste gas outlet (74).

2. The environment-friendly sludge pyrolysis apparatus as claimed in claim 1, wherein the condensation washing assembly (84) comprises a spray header (79) and a pall ring (80), the spray header (79) is arranged at the top of the washing chamber (76), and the pall ring (80) is filled in the washing chamber (76); the bottom of the condensing chamber (83) is a liquid leakage pore plate, a storage tank (85) for storing an oil-water mixture is arranged below the condensing chamber (83), and the spray header (79) is communicated with a water storage tank (81).

3. The environment-friendly sludge pyrolysis apparatus as claimed in claim 2, wherein the gas storage tank (30) stores liquefied gas.

4. The environment-friendly oil sludge pyrolysis equipment as claimed in claim 2, wherein a second liquid phase outlet (91) is formed in the upper portion of the storage tank (85), the second liquid phase outlet (91) is communicated with the oil-water separation equipment (87), a crude oil outlet (89) and a wastewater outlet (90) are formed in the oil-water separation equipment (87), and the wastewater outlet (90) is communicated with the water storage pool (81).

5. The environment-friendly oil sludge pyrolysis equipment as claimed in claim 1, wherein the cold air outlet (21) is communicated with a heated air circulating fan (33), an air outlet pipe (34) is arranged on the heated air circulating fan (33), a refrigerant inlet (38) is arranged on the heat exchanger (36), and the air outlet pipe (34) is communicated with the refrigerant inlet (38).

6. The environment-friendly oil sludge pyrolysis equipment as claimed in claim 1, wherein a driving shaft (23) is rotatably connected in the casing (18), a first paddle (26) is arranged on the driving shaft (23), the first paddles (26) are arranged in a plurality along the axial direction of the driving shaft (23), and the first paddles (26) are spirally and discontinuously arranged.

7. The environment-friendly sludge pyrolysis equipment as claimed in claim 6, wherein the casing (18) is rotatably connected with a driven shaft (24), the driving shaft (23) is provided with a driving gear (46), and the driven shaft (24) is provided with a driven gear (47) engaged with the driving gear (46); be equipped with second paddle (103) on driven shaft (24), second paddle (103) are equipped with a plurality ofly along the axis direction of driven shaft (24), and are a plurality of second paddle (103) are the heliciform and are interrupted the setting, first paddle (26) and second paddle (103) crisscross the setting.

8. The environment-friendly sludge pyrolysis equipment as claimed in claim 1, wherein the feed inlet (41) is communicated with a sludge washing tank (9) for adding a sludge washing dispersant, an extension stirring shaft (93) is rotatably connected in the sludge washing tank (9), and a sludge stirring blade (10) is connected on the extension stirring shaft (93).

9. An environment-friendly sludge pyrolysis apparatus as claimed in any one of claims 1 to 8 wherein the outside of the sandwiched casing (27) is coated with an insulating layer (22).

10. The environment-friendly sludge pyrolysis apparatus as claimed in any one of claims 1 to 8, wherein a plurality of flow deflectors (94) are disposed in the heating chamber (19), the flow deflectors (94) are disposed along the length direction of the casing (18), two sides of the plurality of flow deflectors (94) are respectively attached to the casing (18) and the interlayer casing (27), hot air through holes (95) are disposed between one end of each flow deflector (94) and the casing (18), and the hot air through holes (95) on two adjacent flow deflectors (94) are staggered.

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