CN211360026U - Oily solid waste electromagnetic heating indirect thermal desorption treatment device - Google Patents
Oily solid waste electromagnetic heating indirect thermal desorption treatment device Download PDFInfo
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- CN211360026U CN211360026U CN201921887229.6U CN201921887229U CN211360026U CN 211360026 U CN211360026 U CN 211360026U CN 201921887229 U CN201921887229 U CN 201921887229U CN 211360026 U CN211360026 U CN 211360026U
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Abstract
The utility model provides an indirect thermal desorption processing apparatus of oily solid useless electromagnetic heating is including the automatic control unit, through the feeding preprocessing unit that oily solid waste material transfer mode communicates according to the preface, dosing and protection unit, the indirect thermal desorption unit of electromagnetic heating, the thermal desorption vapour processing unit who connects in the indirect thermal desorption unit exhaust port department of electromagnetic heating, be connected with thermal desorption vapour processing unit and provide the condensate processing unit of cooling medium for the cooling, and the ejection of compact cooling conveying unit who connects in the indirect thermal desorption unit discharge port department of electromagnetic heating. The electromagnetic heating indirect thermal desorption unit comprises one group or more than one group of thermal desorption cavity devices which are arranged in parallel, each group of thermal desorption cavity device comprises two or more than two thermal desorption cavities which are connected in series, and the thermal desorption cavities at all the stages are arranged in a layered mode and are connected end to end. The thermal desorption steam output by each thermal desorption cavity is subjected to fractional directional condensation and recovery by the thermal desorption steam processing unit.
Description
Technical Field
The utility model relates to an indirect thermal desorption processing apparatus of oily solid useless electromagnetic heating is applicable to the innocent treatment of oil base detritus, organic contaminated soil, the oily soil of light that oil field drilling exploitation and shale gas development produced.
Background
Oil-based rock debris produced in the production processes of oil drilling, shale gas development and the like, organic contaminated soil produced in operation, light oil-immersed soil and the like belong to solid wastes containing oil, and are various in types, complex in components, large in annual output, large in environmental hazard and large in treatment technology difficulty. The current harmless treatment technology of oil-containing solid waste is mainly thermal washing, burning and thermal desorption technology. Resources can be recycled through hot washing, but the oil content of the sludge after hot washing still hardly reaches the harmless index required by the state, and a large amount of generated wastewater needs to be subjected to secondary treatment; the harmless effect of the incineration technology is the best, but the requirement on the water content of the raw materials is higher, and a large amount of incineration tail gas is difficult to treat, so that secondary pollution to the atmosphere is easily caused; the thermal desorption technology can recycle resources while completing the harmless treatment effect, has no secondary pollution, and has more advantages in the aspects of safety, environmental protection, resource recovery and the like.
The thermal desorption treatment technology is mainly characterized in that the sludge in the oil field is heated to a sufficient temperature, volatile hydrocarbon substances (oil) are volatilized and separated from the sludge, and the soil is purified. The separated volatile hydrocarbon is reprocessed for reuse or discharged by combustion. Compared with other technologies, the thermal desorption technology has the advantages of high efficiency, rapidness, no secondary pollution, safety and guarantee of reaching harmless indexes. The thermal desorption treatment technology is divided into indirect thermal desorption and direct thermal desorption, and the difference between the indirect thermal desorption and the direct thermal desorption is that a heating medium is not directly contacted with a material, so that the thermal desorption treatment can be carried out under the closed anoxic or anoxic condition, the production is safer, the generated thermal desorption steam is less, and the treatment is easy.
At present, the widely adopted indirect thermal desorption method mainly heats fuel gas and fuel oil, mostly adopts a single-layer station type construction mode, mainly sprays and washes generated thermal desorption gas, has certain dependence on fuel sources, occupies a large area of the whole device, is complex to install, has low quality of recovered oil, has complex water treatment process, and is not suitable for being used in production fields of sensitive areas with high fire protection requirements.
SUMMERY OF THE UTILITY MODEL
In order to solve the problem, the utility model aims to provide a do not have naked light, high integration degree, sled piece ization arrange, retrieve oil quality height, the oil base detritus that is applicable to oil field well drilling exploitation and shale gas development production of waste water easy processing, organic contaminated soil and the oily innocent treatment's of light device and technique of soil that soaks.
The utility model comprises an automatic control unit, a feeding pretreatment unit, a quantitative feeding and protecting unit, an electromagnetic heating indirect thermal desorption unit, a thermal desorption steam treatment unit, a condensate treatment unit and a discharging cooling conveying unit which are communicated in sequence in the oil-containing solid waste material conveying mode,
a feed port of the electromagnetic heating indirect thermal desorption unit is sequentially connected with the quantitative feeding and protecting unit and the feeding pretreatment unit, an exhaust port of the electromagnetic heating indirect thermal desorption unit is connected with the thermal desorption steam treatment unit, and a discharge port of the electromagnetic heating indirect thermal desorption unit is connected with the discharged material cooling conveying unit;
the thermal desorption steam processing unit is connected with the condensate processing unit which provides a cooling medium for the thermal desorption steam processing unit;
the electromagnetic heating indirect thermal desorption unit comprises one or more groups of thermal desorption cavity devices which are arranged in parallel, each group of thermal desorption cavity device comprises two or more stages of thermal desorption cavities which are connected in series, each stage of thermal desorption cavity is provided with a feed inlet, a discharge outlet and an exhaust outlet, each stage of thermal desorption cavity is correspondingly provided with a driving device, each stage of thermal desorption cavity and the corresponding driving device are assembled on the same frame together, the frames of the thermal desorption cavities are fixedly connected, and then the thermal desorption cavities are arranged from top to bottom in layers, wherein the discharge outlet of the thermal desorption cavity at the upper stage is hermetically connected with the feed inlet of the thermal desorption cavity at the lower stage, so that the thermal desorption cavities at the upper stage are connected end to end;
an air inlet pipeline of the thermal desorption steam processing unit is connected to an air outlet at the top of each stage of the thermal desorption cavity, and the thermal desorption steam entering the thermal desorption steam processing unit is purified and recycled;
and a discharge hole of the last stage thermal desorption cavity of the electromagnetic heating indirect thermal desorption unit is connected with the discharge cooling conveying unit.
Preferably, after the thermal desorption cavity devices are arranged in parallel, the feed inlets of all the first-stage thermal desorption cavities are connected with one dosing and protecting unit, and the discharge outlets of all the last-stage thermal desorption cavities are connected with one discharged material cooling and conveying unit.
Preferably, each stage of the thermal desorption cavity comprises a closed cylinder, an air collection cavity which is arched upwards is arranged in the middle of the top of the cylinder along the axial direction of the cylinder, and the wall surface of the air collection cavity is tangentially connected with the wall surface of the cylinder.
Preferably, the outer surfaces of the cylinder and the gas collection cavity are covered with heat insulation layers, multiple groups of electromagnetic induction heating cables are wound in the outer sub-areas of the heat insulation layers in a directional mode, a plurality of thermocouples are arranged outside the wall surface of the cylinder and the wall surface of the gas collection cavity, and the electromagnetic induction heating cables in each sub-area and the thermocouples form a control loop.
Preferably, a group of screw propellers with material turning plates and cleaning chains are arranged inside the cylinder of each stage of thermal desorption cavity, one end of each screw propeller extends out of the cylinder and is connected with the driving device, and a driving shaft of the driving device and the cylinder are sealed and sealed by filling materials.
Preferably, the discharge hole of the last stage of the thermal desorption cavity is connected with an air lock device, and the air lock device is a double-turning plate type or star-shaped rotary air lock device.
Preferably, the feeding pretreatment unit uses a vibrating screen, a crusher, a rock debris dryer, a centrifuge, a storage tank and a feeder or uses a crusher, a vibrating screen, a magnetic separator and a feeder according to the characteristics of the oil-containing solid waste.
Preferably, the thermal desorption steam processing unit comprises a cyclone separator, a first-stage condenser, a second-stage condenser, a fan, an alkali liquor absorption tower and an activated carbon tank which are sequentially communicated through pipelines according to the thermal desorption steam flow sequence, wherein the first-stage condenser and the second-stage condenser are connected with a cooler and the condensate processing unit through pipelines.
Preferably, cyclone is including being the closed casing of tubbiness, inside from last gas distribution district, disengagement zone, gas collection district and the dust collection district of down being formed with in proper order of closed casing, gas distribution district is provided with the follow casing lateral wall tangential gets into can the casing internal energy forms the gas inlet that whirlwind formula admitted air, the top of casing is provided with gas outlet, gas outlet is the straight-through extension and enters into upright tube in the gas collection district, the bottom of casing is provided with the discharge gate, the discharge gate is connected the dust collection district.
Preferably, the condensate treatment unit comprises an oil water treatment device, the oil water treatment device comprises a recovered oil buffer tank, a recovered oil tank, an oil-water separation tank and a recovered water tank, and a heat exchange tube is arranged in the recovered oil buffer tank; an oil receiving groove or a floating oil receiver for recovering floating oil in the condensed water is arranged in the oil-water separation tank; the bottom parts of the recovered oil buffer tank and the oil-water separation tank are provided with sludge discharge pipes, the recovered oil tank is communicated with a cooling medium inlet of the primary condenser through a pipeline, and a cooling medium outlet of the primary condenser is communicated with the recovered oil buffer tank; the recovery water tank is communicated with a cooling medium inlet of the secondary condenser through a pipeline, and a cooling medium outlet of the secondary condenser is communicated with the oil-water separation tank.
The electromagnetic heating indirect thermal desorption treatment device for the solid waste containing oil of the utility model obtains relatively homogeneous materials suitable for indirect thermal desorption treatment through the feeding pretreatment unit; the continuous and stable operation of the whole device is ensured by the constant feeding amount of the quantitative feeding and protecting unit; the separation of oil, water and a solid phase is realized through an electromagnetic heating indirect thermal desorption unit, and the harmlessness of the solid phase is realized; the thermal desorption steam treatment unit and the condensate treatment unit realize heat balance, oil resource recovery and non-condensable gas utilization, and ensure that the residual sewage does not pollute the environment; the discharging, cooling and conveying unit realizes solid-phase cooling and avoids dust raising.
The utility model discloses utilize the multistage directional condensation in grades among the thermal desorption vapour processing unit, retrieve the processing mode of repurifying, solved the problem that the polluted water volume that sprays the washing mode and cause is big, water treatment process is complicated, and directional recovery oil quality is high and need not extra processing, and the clear water consumption is extremely low, and follow-up recovery water volume is little and the easy processing, equipment easy operation, and the operation is reliable and stable.
Drawings
Fig. 1 is a schematic block diagram of the electromagnetic heating indirect thermal desorption treatment device for the solid waste containing oil of the utility model.
Fig. 2 is a first flow chart of the feed pretreatment unit of the present invention.
Fig. 3 is a flow chart of the middle feed pretreatment unit of the present invention.
Fig. 4 is a schematic structural diagram of the indirect thermal desorption unit of the middle electromagnetic heating system of the present invention.
Fig. 5 is a schematic structural diagram of the indirect thermal desorption unit of the middle electromagnetic heating system of the present invention.
Fig. 6 is a schematic sectional view of the heat desorption chamber of the present invention.
Fig. 7 is a schematic structural view of the thermal desorption steam treatment unit and the condensate treatment unit of the present invention.
Fig. 8 is a schematic structural diagram of the cyclone separator of the present invention.
Description of the main figures:
1 feed pretreatment unit, 2 quantitative feeding and protecting unit, 3 electromagnetic heating indirect thermal desorption unit, 4 thermal desorption steam treatment unit, 5 condensate treatment unit, 6 discharge cooling conveying unit, 7 automatic control unit, 8 storage bin, 9 level sensor, 10 double-screw feeder, 11 thermal desorption cavity, 12 gas collection cavity, 13 heat preservation layer, 14 heating cable, 15 thermocouple, 16 screw propeller, 17 variable frequency speed reduction motor, 18 airlock device, 19 water cooling jacket conveyor, 20 humidifier, 21 nozzle, 22 humidifier outlet, 23 slag receiving hopper, 24 cyclone separator, 25 primary condenser, 26 secondary condenser, 27 fan, 28 alkali absorption tower, 29 active carbon tank, 30 cooler, 31 filter, 32 centrifuge, 33 oil water treater, 34 vibrating screen, 35 crusher, 36 debris drying machine, 37 centrifuge, 38 box, 39 feeding machine, 40 magnetic force sorter. 41 feeding pipes, 42 discharging ports, 43 feeding ports, 44 vertical pipelines, 45 metal steel frames, 46 variable-frequency speed reducing motors, 47 discharging ports of thermal desorption chambers, 48 exhaust ports, 50 shells, 51 first shells, 52 second shells, 53 gas inlets, 54 gas locking devices, 55 discharging ports, 56 gas outlets, 60 recovered oil buffer tanks, 61 oil-water separators, 62 recovered oil tanks, 63 heat exchange coil pipes, 64 recovered water tanks, 65 mud discharge pipes, 66 oil pipes and 67 water pipes
Detailed Description
The following detailed description of the embodiments of the present invention will be made with reference to the accompanying drawings.
As shown in fig. 1, the utility model discloses the indirect thermal desorption processing apparatus of well oiliness solid useless electromagnetic heating is including: the device comprises an automatic control unit 7 which is unified and coordinated, a feeding pretreatment unit 1, a quantitative feeding and protecting unit 2, an electromagnetic heating indirect thermal desorption unit 3, a thermal desorption steam treatment unit 4, a condensate treatment unit 5 and a discharging cooling conveying unit 6 which are sequentially communicated in an oil-containing solid waste material conveying mode. Wherein:
the electromagnetic heating indirect thermal desorption unit 3 heats the indirect thermal desorption cylinder through electromagnetic induction and transfers heat to the material in the thermal desorption cylinder, so that indirect heating is realized. The feed inlet of the electromagnetic heating indirect thermal desorption unit 3 is sequentially connected with the quantitative feeding and protecting unit 2 and the feeding pretreatment unit 1, the exhaust port of the electromagnetic heating indirect thermal desorption unit 3 is connected with the thermal desorption steam treatment unit 4, and the discharge port of the electromagnetic heating indirect thermal desorption unit 3 is connected with the discharge cooling conveying unit 6. The thermal desorption steam processing unit 4 is connected with the condensate processing unit 5, and the condensate processing unit 5 provides a cooling medium for cooling the thermal desorption steam processing unit 4. Specifically, the method comprises the following steps:
as shown in fig. 2 and 3, the feeding pretreatment unit 1 is used for pretreatment before the oil-containing solid waste material is produced, because the components of the oil-containing solid waste material are different, different devices are required to be selected for treatment.
If the oily solid waste material is oil-based rock debris, the vibrating screen 34 and the crusher 35 shown in fig. 2 are selected to control the feeding particle size, the rock debris drier 36 and the centrifuge 37 are used to control the liquid content of the material, and the processed oily solid waste material is conveyed to the storage box 38 for storage and then conveyed to the dosing and protecting unit 2 through the feeding machine 39.
If the oily solid waste material is organically polluted soil or light oil-immersed soil, the crusher 35 and the vibrating screen 34 shown in fig. 3 are selected to control the feeding particle size, the magnetic separator 40 is used for removing iron-containing impurities, and the treated oily solid waste material is conveyed to the quantitative feeding and protecting unit 2 by the feeding machine 39.
Preferably, as shown in fig. 5, the dosing and protecting unit 2 is fixedly installed on the top of the electromagnetic heating indirect thermal desorption unit 3 through a metal steel frame 45, and includes a conical hopper storage bin 8, as shown in fig. 4, a plurality of level sensors 9 for controlling the material layer height are disposed on the sidewall of the storage bin 8, a feeding pipe 41 communicated with the storage bin 8 is disposed at the bottom of one side of the storage bin 8, a discharge port 42 is disposed at the bottom of the feeding pipe 41, and the discharge port 42 is communicated with a feeding port 43 of the electromagnetic heating indirect thermal desorption unit 3 through a vertical pipe 44. A nitrogen gas inlet is provided at the outlet 42, and the inert gas protection of the system is realized by introducing nitrogen gas, which is a prior art and will not be described in detail herein.
Preferably, the bottom of the storage bin 8 is provided with a double-screw feeder 10 with a self-cleaning function, and the double-screw feeder 10 extends into the feeding pipe 41 and is driven by a variable-frequency speed reduction motor 46 arranged outside the storage bin 8. The utility model provides a rotary propelling movement oiliness solid waste material of storage silo 8 through double helix feeder 10 to control feeding volume under the condition of inert gas protection. Meanwhile, the sealing of the oil-containing solid waste material is realized by controlling the height of the material layer, the quantitative feeding of the electromagnetic heating indirect thermal desorption unit 3 is realized by adjusting the rotating speed through an automatic control program in the automatic control unit 7, and no gas enters during feeding, so that the electromagnetic heating indirect thermal desorption unit 3 is ensured to be processed in an anaerobic state.
As shown in fig. 4 and 5, the electromagnetic heating indirect thermal desorption unit 3 in this embodiment includes four thermal desorption cavities 11, each thermal desorption cavity 11 is a stage, each stage of thermal desorption cavity 11 corresponds to a driving device, the driving device is a variable frequency speed reduction motor 17, each stage of thermal desorption cavity 11 and the driving device are together and fixedly mounted on a metal steel frame (or a frame made of other materials) 45, so as to form an independent pry convenient for assembly and disassembly. The two-stage thermal desorption cavities 11 are vertically overlapped to form a group of thermal desorption cavity devices by vertically fixing the metal steel frame 45 in parallel, and the two groups of thermal desorption cavity devices are arranged in parallel from left to right through the metal steel frame 45 to form the complete electromagnetic heating indirect thermal desorption unit 3 in the embodiment. As shown in fig. 5, the feeding ports 43 of all the first-stage thermal desorption chambers 11 in the two sets of thermal desorption chamber devices of the present embodiment are connected to a dosing and protecting unit 2, and the discharging ports 47 of all the last-stage thermal desorption chambers 11 are connected to a discharging temperature-reducing conveying unit 6.
The method comprises the following steps: each thermal desorption cavity 11 comprises a cylinder body with a closed cavity formed in the middle, a feeding hole 43 and a discharging hole 47 are respectively arranged at two ends of the cylinder body, a spiral propeller 16 with a material turning plate and a cleaning chain is arranged in the cavity of the cylinder body and used for pushing oily solid waste materials entering the thermal desorption cavity 11 to move forward, and the speed of the oily solid waste materials moving forward is controlled by an automatic control unit 7 to be driven to rotate by a variable-frequency speed-reducing motor 17 arranged outside one end of the cylinder body in a unified mode. As shown in fig. 4, after the two stages of thermal desorption chambers 11 are vertically stacked and arranged in parallel from top to bottom through the metal steel frame 45, the discharge port 47 of the upper stage of thermal desorption chamber 11 is hermetically connected with the feed port 43 of the lower stage of thermal desorption chamber 11, the discharge port 47 of the last stage of thermal desorption chamber 11 is connected with the airlock device 18 and then connected with the discharge cooling and conveying unit 6, wherein the airlock device 18 can be in a double-turnover plate type or star-shaped rotating type, and nitrogen is introduced for protection.
As shown in fig. 4 and 6, each thermal desorption cavity 11 is formed with an upward-arched gas collection cavity 12 at the top of the sealed cylinder along the axial direction of the cylinder, the length of the gas collection cavity 12 is 70% -80% of the length of the cylinder, two side walls of the gas collection cavity 12 are tangentially connected with the cylinder wall, so that all gas generated after heating the oil-containing solid waste material in the cylinder enters the gas collection cavity 12, high pressure is not formed in the cylinder, the gas is output to the thermal desorption steam treatment unit 4 through a gas outlet 48 at the top of the gas collection cavity 12, and the gas outlet 48 at the top of each gas collection cavity 12 is connected with the desorption steam treatment unit 4 through a pipeline.
The cylinder body and the gas collection cavity 12 are covered with a heat preservation layer 13 which takes ceramic fiber cotton as a main body and is covered with glass fiber cloth, a plurality of groups of electromagnetic induction heating cables 14 are directionally wound outside the heat preservation layer 13 in regions, a plurality of thermocouples 15 are arranged outside the wall surface of the cylinder body and the wall surface of the gas collection cavity 12, the electromagnetic induction heating cables 14 and the thermocouples 15 in each region form a control loop, the electromagnetic induction heating cables 14 in each region are independently controlled by an automatic control unit 7, so that the electromagnetic induction heating cables 14 can be respectively controlled by the automatic control unit 7 to heat the cylinder body, the heating cylinder body can be independently controlled in regions, the temperature inside the cylinder body is different, as shown in figure 4, the thermal desorption cavity 11 is divided into two regions, two sections of different temperatures can be provided in one thermal desorption cavity 11, so that oil-containing solid waste materials enter different temperature regions to realize water vapor evaporation while moving in the thermal desorption cavity 11, oil desorption process, etc.
The spiral propeller 16 arranged in the thermal desorption cavity 11 comprises a driving shaft connected with a variable-frequency speed reducing motor 17, the driving shaft extends out of the cylinder body and is driven by the variable-frequency speed reducing motor 17, and the driving shaft and the cylinder body are sealed and sealed by using a filler to prevent gas leakage. The sealing between the cylinder and the drive shaft, and the air lock device 18 and the sealing connection between the air lock device 18 and the cylinder are well known in the art and will not be described in detail herein. The spiral propeller 16 also comprises spiral blades fixedly arranged on the driving shaft, the spiral blades are arranged in a variable pitch mode, namely, the intervals among all the spiral blades are unequal, and in the initial stage of thermal desorption, the water content and the oil content of the material are high, the volume of the material is large, and the material is a large-interval spiral blade; in the middle and later stages of thermal desorption, along with the desorption separation of water and oil, the volume of residue is reduced, and helical blades with reduced spacing are selected. The spiral blades of the spiral propeller 16 are provided with material turning plates which can turn and mix the materials while propelling the materials to move forward, so that the materials are uniformly heated. The spiral propeller 16 is also provided with a cleaning chain which rotates along with the spiral propeller 16 and simultaneously collides with the spiral blades by means of the self gravity of the chain links, so that the spiral blades are cleaned.
The utility model discloses the quantity of thermal desorption chamber device in the indirect thermal desorption unit 3 of well electromagnetic heating and the quantity of thermal desorption chamber in each group thermal desorption chamber device can be set for as required the volume of the solid waste material of oiliness of handling to be not limited to the quantity of thermal desorption chamber 11 and the quantity of thermal desorption chamber device in this embodiment.
The utility model discloses well oily solid useless electromagnetic heating indirect thermal desorption processing apparatus passes through metal steelframe 45 and with multistage thermal desorption cavity series connection to top-down average stack setting, it is few to have the ground space of boring, the advantage that throughput is strong, and can make things convenient for the equipment and the connection in thermal desorption chamber, can set up the thermal desorption chamber of a plurality of differences according to the handling capacity of oily solid waste material, or the indirect thermal desorption unit 3 of a plurality of electromagnetic heating, be applicable to the oil field of different scales.
Under airtight condition, the utility model provides an electromagnetic heating indirect thermal desorption unit 3 utilizes 14 indirect heating thermal desorption chambeies 11 of electromagnetic induction heating cable, and the solid waste material of oiliness is in the inside indirect heating of thermal desorption chamber 11 barrel and is accomplished the thermal desorption reaction. Specifically, under the control of the automatic control unit 7, the helical propeller 16 arranged inside the thermal desorption cavity 11 with the cylindrical structure pushes the oily solid waste materials to advance, so that the total retention time of the oily solid waste materials in all the thermal desorption cavities is 15-45 min, and the optimal retention time is 20-40 min. Meanwhile, the automatic control unit 7 controls the temperature of each area in the thermal desorption cavity 11 to realize the automatic independent temperature control of each subarea, so that the heating temperature of the thermal desorption cavity 11 can be automatically set between 100 ℃ and 550 ℃ according to the characteristics of the oil-containing solid waste materials. Thereby completing the full thermal desorption treatment according to the characteristics of different oil-containing solid waste materials.
As shown in fig. 5, the discharging, cooling and conveying unit 6 is used for hermetically conveying high-temperature residue soil treated by the electromagnetic heating indirect thermal desorption unit 3, and includes a conveyor 19 with a water cooling jacket, and is connected with an air lock device 18 at a discharge port 47 of the electromagnetic heating indirect thermal desorption unit 3. The conveyer 19 selects a screw conveyer, a buried scraper conveyer or a pipe chain conveyer according to the material properties, the conveyer 19 can be horizontally or obliquely arranged according to the elevation requirement, a bucket elevator can be additionally arranged for lifting when necessary, and the conveyer 19 can realize indirect heat exchange and cooling on the material while carrying out closed conveying by utilizing a water cooling jacket outside the conveyer 19. The outlet of the conveyor 19 is connected with a humidifier 20, the humidifier 20 can be a single-shaft or double-shaft humidifier, the top of the humidifier is provided with a nozzle 21 which can spray clean water to humidify, cool and suppress dust of the residue soil, the outlet 22 of the humidifier is aligned with the residue receiving hopper 23, and the residue soil after being humidified and cooled is discharged into the residue receiving hopper 23 or bagged for external transportation. All the devices in the discharging, cooling and conveying unit 6 adopt commercially available mature products, and the detailed description is omitted.
As shown in fig. 1 and 7, the thermal desorption steam treatment unit 4 is used for performing separation and dust removal, fractional condensation and recovery, purification and adsorption treatment on thermal desorption steam exhausted from the gas collection cavity 12 of the electromagnetic heating indirect thermal desorption unit 3 until the thermal desorption steam reaches the standard, and then discharging the thermal desorption steam out or recycling the thermal desorption steam. Specifically, under the suction action of the fan 27, the thermal desorption steam processing unit 4 sequentially enters the cyclone separator 24 for separation and dust removal from the gas collection chamber 12, the primary condenser 25 is used for directionally recovering volatile hydrocarbons (oil), the secondary condenser 26 is used for recovering cooling water, the cooling water is discharged into the alkali liquor absorption tower 28 for removing acid gas and the activated carbon tank 29 for absorption and purification treatment until the oil and the water reach the standard, and the oil and the water recovered by the primary and secondary condensers enter the condensate processing unit 5. Wherein, the first-stage condenser 25 and the second-stage condenser 26 can select a spray type direct heat exchange condenser or a shell-and-tube heat exchanger type indirect heat exchange condenser according to the heat exchange quantity and the medium characteristics.
Preferably, the thermal desorption steam treatment unit 4 comprises a cyclone separator 24, a primary condenser 25, a secondary condenser 26, a fan 27, an alkali liquor absorption tower 28 and an activated carbon tank 29 which are sequentially communicated through pipelines according to the thermal desorption steam flow, wherein the primary condenser 25 and the secondary condenser 26 are connected with a cooler 30 and the condensate treatment unit 5 through pipelines.
As shown in fig. 7, the thermal desorption steam treatment unit 4 in this embodiment uses a fan 27 as a power source for gas movement, and is disposed on a gas pipeline between the secondary condenser 26 and the lye absorption tower 28, and negative pressure vacuum is generated in the gas pipeline at the front end of the fan 27 due to suction, and positive pressure exhaust is formed in the gas pipeline at the rear end of the fan 27. The thermal desorption gas (hereinafter also referred to as gas) from the electromagnetic heating indirect thermal desorption unit 3 tangentially enters the cyclone separator 24 in a cyclone form at the wind speed of 15-25m/s under the action of the fan 27, under the action of centrifugal force, heavy solid dust particle impurities cling to the inner wall of the equipment to do high-speed centrifugal motion and fall into a dust collecting chamber at the bottom of the cyclone separator in a rotating manner, the separation of gas and solid particles is realized in the cyclone separator 24, the gas with dust particles removed is discharged from the top of the cyclone separator 24 and then enters the first-stage condenser 25 in sequence, the first-stage condenser 25 adopts a spray tank condenser which takes cooling oil as a cooling medium for direct heat exchange, the exhaust temperature in the first-stage condenser 25 is 120 ℃, the volatile hydrocarbon substances in the hot desorption steam in the first-stage condenser 25 are condensed into liquid oil and discharged into the condensate treatment unit 5, and the rest gas enters the second-stage condenser 26. The secondary condenser 26 is a shell-and-tube heat exchanger using cooling water as a cooling medium for indirect heat exchange. The exhaust temperature in the secondary condenser 26 was 80 ℃. The gas is cooled in the first-stage condenser 25 and the second-stage condenser 26 in a fractional manner, then enters an alkali liquor absorption tower 28, the alkali liquor absorption tower 28 is washed by alkali liquor to remove acidic harmful impurities, and finally is adsorbed and purified by an activated carbon tank 29 to reach the emission standard; the cooling medium for the first-stage condenser 25 and the second-stage condenser 26 is obtained from the water treatment device 33 in the condensate treatment unit 5 by an oil pump or a water pump, and the cooling medium obtained from the water treatment device 33 is subjected to cooling treatment by the cooler 30 when entering and/or exiting the first-stage condenser 25 and the second-stage condenser 26, so that the temperature of the cooling medium entering the first-stage condenser 25 and the second-stage condenser 26 is ensured, and effective cooling treatment is performed on the gas.
As shown in fig. 8, the cyclone separator 24 includes a closed casing 50 having a barrel shape, and the closed casing 50 has a gas distribution area, a separation area, a gas collection area and a dust collection area formed therein from top to bottom, and preferably, the casing 50 is made of a high temperature resistant and wear resistant metal, such as carbon steel or stainless steel. Specifically, the shell 50 includes a first shell 51 in a cylindrical shape and a second shell 52 in an inverted conical shape, the first shell 51 is hermetically connected with the second shell 52, a spiral gas inlet 53 is arranged at the top of the first shell 51, the spiral gas inlet 53 is tangentially connected with the side wall of the top of the first shell 51, so that the thermal desorption gas entering from the gas inlet 53 enters the shell 50 in a spiral (also called cyclone) manner, and a gas distribution area is formed. A separation area is formed in the first housing 51, a gas collection area is formed at the connection of the first housing 51 and the second housing 52, and a dust collection area is formed inside the second housing 52. The second housing 52 is provided with a gas lock 54 and a discharge hole 55 at the bottom, and a gas outlet 56 is hermetically arranged at the middle position of the top of the first housing 51, wherein the gas outlet 56 is a vertical pipe hermetically connected with the first housing 51, and the vertical pipe extends from the top of the first housing 51 into the first housing 51 and extends to the position where the first housing 51 is connected with the second housing 52 to the gas collection area.
As shown in fig. 7, the condensate treatment unit 5 includes an oil water treatment device 33 for recovering and reprocessing the oil and water condensed and recovered by the thermal desorption steam treatment unit 4, respectively. Specifically, the oil water treatment device 33 is divided into 4 functional tanks, which are a recovered oil buffer tank 60, a recovered oil tank 62, an oil-water separation tank 61, and a recovered water tank 64. The recovered oil buffer tank 60 is communicated with the recovered oil tank 62 in an overflow manner, and the oil-water separation tank 61 is also communicated with the recovered water tank 64 in an overflow manner. An oil pipe 66 connected with the primary condenser 25 is inserted below the liquid level of the recovered oil buffer tank 60 to receive the condensed water and cooling oil recovered by the primary cooler 25, a heat exchange coil 63 is arranged in the oil pipe, a sludge discharge pipe 65 connected with the centrifuge 32 is arranged at the bottom of the oil pipe, circulating cooling water is introduced into the heat exchange coil 63 to perform heat exchange and cooling treatment on the recovered oil, and the cooled oil and water overflow to the recovered oil tank 62 for storage.
The water pipe 67 connected with the secondary condenser 26 is inserted under the liquid level of the oil-water separation tank 61 to receive the condensed water recovered in the secondary cooler 3, a fixed or floating oil receiver (not shown in the figure) is arranged in the condensed water pipe, a mud pipe 65 is arranged at the bottom of the condensed water pipe to perform secondary oil removal and purification treatment on the recovered condensed water, the discharged oil enters the recovery oil tank 62 for cooling treatment of the primary condenser 25, the water enters the recovery water tank 64 in an overflow mode for cooling the secondary condenser 26, and the water is periodically discharged to the filter 31 to be treated and output after reaching the standard. The oil water treatment device 33 specifically comprises the following use processes:
the liquid oil recovered from the primary condenser 25, including condensed water, enters the recovered oil buffer tank 60 together, exchanges heat and cools under the action of the heat exchange tube 63 in the recovered oil buffer tank 60, and overflows to the recovered oil tank 62 for storage; the condensed water recovered from the secondary condenser 26 enters an oil-water separation tank 61 having an oil receiver to perform secondary oil collection, and then overflows to a recovery water tank 64 to be stored. The recovered oil buffer tank 60 and the oil-water separation tank 61 discharge the sludge collected at the bottom into the centrifuge 32 through the arranged sludge discharge pipe 65 for subsequent treatment.
The solid sludge separated by the centrifuge 32 returns to the dosing and protecting unit 2 for retreatment, and the liquid mixture is conveyed to the oil-water separation tank 61 for retreatment. The associated cooler 30 carries excess heat away from the system by indirect heat exchange.
To sum up, the utility model discloses the indirect thermal desorption processing apparatus of well oiliness solid useless electromagnetic heating has following advantage:
1) adopt electromagnetic induction heating to the material heating method, whole process does not have naked light, isolated air is safer, and the material is inside and outside two-way to be heated simultaneously, and heat transfer efficiency is high, and whole device arranges compactly, and the modularization degree is high, and the installation is demolishd the work load few, practices thrift and takes up an area of, arranges in a flexible way.
2) The method adopts a multi-stage grading directional condensation recovery and re-purification treatment mode for thermal desorption steam, solves the problems of large polluted water amount and complex water treatment process caused by spray washing, has high quality of directional recovered oil, does not need additional treatment, has extremely low clear water consumption, small subsequent recovered water amount, easy treatment, simple equipment operation and stable and reliable operation.
3) The thermal desorption cavity of the electromagnetic heating indirect thermal desorption unit can set different control temperatures according to different functions of the actual stage, for example, the control temperature in the dehydration section is between 150 and 250 ℃, and the control temperature in the oil vapor volatilization section is between 350 and 550 ℃, so as to realize fixed-point collection for different materials and avoid energy waste caused by overhigh temperature rise of water vapor.
4) The utility model provides an automatic control unit concentrates on all online various flow, pressure, temperature, liquid level of unit, rotating equipment rotational speed, motor operating frequency, motor current and voltage and automatic control valve state etc. and shows, reports to the police and control to be equipped with automatic control program and accomplish the operation, be equipped with the chain control program and guarantee unit operation safety, be equipped with data acquisition memory function and generate the statement in order to look up historical data. The control of the whole device is realized through DCS or PLC, the flow of each unit, the real-time state of a control point and the real-time data of a monitoring point are displayed on a computer screen, and the operation control of the units and the setting of automatic control program parameters can be realized on a display screen.
5) The utility model discloses the total petroleum hydrocarbon content of solid phase after the processing can reach below 0.3%, ensures stable control under the various operating modes. More than 75% of oil in the oil-containing solid waste is recovered with high quality, the residual sewage is purified, utilized or properly disposed, the non-condensable gas is directly discharged or recycled on site, the tail gas reaches the standard, secondary pollution to the environment is avoided, and the method can be widely applied to harmless treatment of oil-based detritus, organic polluted soil and light oil-immersed soil generated by oil field drilling exploitation and shale gas development.
The foregoing is illustrative of the present invention and is not intended to limit the invention in any way. All the technical points of the present invention are any simple modification, equivalent change and modification made to the above examples, which still fall within the scope of the technical solution of the present invention.
Claims (10)
1. The utility model provides an indirect thermal desorption processing apparatus of oily solid useless electromagnetic heating, is including making unified coordinated automatic control unit, with feeding preprocessing unit, dosing and the protection unit, the indirect thermal desorption unit of electromagnetic heating, thermal desorption vapour processing unit, condensate processing unit and the ejection of compact cooling conveying unit that oily solid waste material transfer mode communicates according to the preface, its characterized in that:
a feed port of the electromagnetic heating indirect thermal desorption unit is sequentially connected with the quantitative feeding and protecting unit and the feeding pretreatment unit, an exhaust port of the electromagnetic heating indirect thermal desorption unit is connected with the thermal desorption steam treatment unit, and a discharge port of the electromagnetic heating indirect thermal desorption unit is connected with the discharged material cooling conveying unit;
the thermal desorption steam processing unit is connected with the condensate processing unit which provides a cooling medium for the thermal desorption steam processing unit;
the electromagnetic heating indirect thermal desorption unit comprises one or more groups of thermal desorption cavity devices which are arranged in parallel, each group of thermal desorption cavity device comprises two or more stages of thermal desorption cavities which are connected in series, each stage of thermal desorption cavity is provided with a feed inlet, a discharge outlet and an exhaust outlet, each stage of thermal desorption cavity is correspondingly provided with a driving device, each stage of thermal desorption cavity and the corresponding driving device are assembled on the same frame together, the frames of the thermal desorption cavities are fixedly connected, and then the thermal desorption cavities are arranged from top to bottom in layers, wherein the discharge outlet of the thermal desorption cavity at the upper stage is hermetically connected with the feed inlet of the thermal desorption cavity at the lower stage, so that the thermal desorption cavities at the upper stage are connected end to end;
an air inlet pipeline of the thermal desorption steam processing unit is connected to an air outlet at the top of each stage of the thermal desorption cavity, and the thermal desorption steam entering the thermal desorption steam processing unit is purified and recycled;
and a discharge hole of the last stage thermal desorption cavity of the electromagnetic heating indirect thermal desorption unit is connected with the discharge cooling conveying unit.
2. The electromagnetic heating indirect thermal desorption treatment device for the oily solid waste according to claim 1, wherein after the thermal desorption cavity devices are arranged in parallel, the feed inlets of all the first-stage thermal desorption cavities are connected with one dosing and protecting unit, and the discharge outlets of all the last-stage thermal desorption cavities are connected with one discharge cooling and conveying unit.
3. The oil-containing solid waste electromagnetic heating indirect thermal desorption treatment device as claimed in claim 1 or 2, wherein each stage of thermal desorption chamber comprises a closed cylinder, an upward arched gas collection chamber is arranged at the middle position of the top of the cylinder along the axial direction of the cylinder, and the wall surface of the gas collection chamber is tangentially connected with the wall surface of the cylinder.
4. The oil-containing solid waste electromagnetic heating indirect thermal desorption treatment device as claimed in claim 3, wherein the outer surfaces of the cylinder and the gas collection cavity are covered with heat insulation layers, a plurality of groups of electromagnetic induction heating cables are wound outside the heat insulation layers in different areas, a plurality of thermocouples are arranged outside the wall surface of the cylinder and the wall surface of the gas collection cavity, and the electromagnetic induction heating cables and the thermocouples in each area form a control loop.
5. The electromagnetic heating indirect thermal desorption treatment device for the oily solid waste according to claim 4, wherein a group of screw propellers with material turning plates and cleaning chains are arranged inside the cylinder of each stage of the thermal desorption cavity, one end of each screw propeller extends out of the cylinder and is connected with the driving device, and a driving shaft of the driving device and the cylinder are sealed and sealed by filling materials.
6. The oil-containing solid waste electromagnetic heating indirect thermal desorption treatment device according to claim 1 or 2, wherein a discharge port of the thermal desorption cavity at the last stage is connected with an air lock device, and the air lock device is a double-turning plate type or star-shaped rotary air lock device.
7. The electromagnetic heating indirect thermal desorption treatment device for the oily solid waste according to claim 1, wherein the feeding pretreatment unit uses a vibrating screen, a crusher, a rock debris drier, a centrifuge, a storage box and a feeding machine or uses a crusher, a vibrating screen, a magnetic separator and a feeding machine according to the characteristics of the oily solid waste.
8. The electromagnetic heating indirect thermal desorption treatment device for the oily solid waste according to claim 1 or 2, wherein the thermal desorption steam treatment unit comprises a cyclone separator, a primary condenser, a secondary condenser, a fan, an alkali liquor absorption tower and an activated carbon tank which are sequentially communicated through pipelines according to the flow sequence of the thermal desorption steam, and the primary condenser and the secondary condenser are connected with a cooler and the condensate treatment unit through pipelines.
9. The electromagnetic heating indirect thermal desorption treatment device for the solid waste containing oil according to claim 8, wherein the cyclone separator comprises a closed casing in a barrel shape, a gas distribution area, a separation area, a gas collection area and a dust collection area are sequentially formed in the closed casing from top to bottom, the gas distribution area is provided with a gas inlet which tangentially enters from the side wall of the casing and can form cyclone-type gas inlet in the casing, the top of the casing is provided with a gas outlet, the gas outlet is an upright pipe which directly extends into the gas collection area, the bottom of the casing is provided with a discharge port, and the discharge port is connected with the dust collection area.
10. The electromagnetic heating indirect thermal desorption treatment device for the oily solid waste according to claim 8, wherein the condensate treatment unit comprises an oil water treatment device, the oil water treatment device comprises a recovered oil buffer tank, a recovered oil tank, an oil-water separation tank and a recovered water tank, and a heat exchange pipe is arranged in the recovered oil buffer tank; an oil receiving groove or a floating oil receiver for recovering floating oil in the condensed water is arranged in the oil-water separation tank; the bottom parts of the recovered oil buffer tank and the oil-water separation tank are provided with sludge discharge pipes, the recovered oil tank is communicated with a cooling medium inlet of the primary condenser through a pipeline, and a cooling medium outlet of the primary condenser is communicated with the recovered oil buffer tank; the recovery water tank is communicated with a cooling medium inlet of the secondary condenser through a pipeline, and a cooling medium outlet of the secondary condenser is communicated with the oil-water separation tank.
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| CN201921887229.6U CN211360026U (en) | 2019-11-05 | 2019-11-05 | Oily solid waste electromagnetic heating indirect thermal desorption treatment device |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113121078A (en) * | 2021-04-13 | 2021-07-16 | 四川省星船城水泥股份有限公司 | Oil-based rock debris resource recycling system |
| CN113135676A (en) * | 2021-04-13 | 2021-07-20 | 四川省星船城水泥股份有限公司 | Anaerobic thermal desorption efficient waste residue treatment method based on oil-based rock debris |
| CN113477692A (en) * | 2021-07-07 | 2021-10-08 | 东南大学 | Organic matter contaminated soil grading thermal desorption and organic matter recycle system |
| US12066251B2 (en) | 2021-03-26 | 2024-08-20 | Jereh Environmental Protection Technology Co., Ltd. | System for treating oily solid material and method for treating oily solid material |
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2019
- 2019-11-05 CN CN201921887229.6U patent/CN211360026U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US12066251B2 (en) | 2021-03-26 | 2024-08-20 | Jereh Environmental Protection Technology Co., Ltd. | System for treating oily solid material and method for treating oily solid material |
| CN113121078A (en) * | 2021-04-13 | 2021-07-16 | 四川省星船城水泥股份有限公司 | Oil-based rock debris resource recycling system |
| CN113135676A (en) * | 2021-04-13 | 2021-07-20 | 四川省星船城水泥股份有限公司 | Anaerobic thermal desorption efficient waste residue treatment method based on oil-based rock debris |
| CN113477692A (en) * | 2021-07-07 | 2021-10-08 | 东南大学 | Organic matter contaminated soil grading thermal desorption and organic matter recycle system |
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