CN209816030U - Continuous distillation and cracking integrated equipment - Google Patents
Continuous distillation and cracking integrated equipment Download PDFInfo
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- CN209816030U CN209816030U CN201920447070.XU CN201920447070U CN209816030U CN 209816030 U CN209816030 U CN 209816030U CN 201920447070 U CN201920447070 U CN 201920447070U CN 209816030 U CN209816030 U CN 209816030U
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Abstract
The utility model relates to a pyrolysis apparatus technical field especially relates to a continuous type distillation schizolysis integration equipment is including the charge-in system who connects gradually, cracking system, oil gas cooling system, circulating water cooling system, still be connected with discharge system and flue gas purification system in the cracking system, circulating water cooling system still is connected with noncondensable combustible gas clean system, the utility model discloses compare more original equipment and reduce heating system, through oil water separator, waste gas utilization has been realized to condensate gas etc. has reduced the pollution to the environment, has improved material utilization, has reduced the pollution to the environment.
Description
Technical Field
The utility model relates to a pyrolysis apparatus technical field especially relates to a continuous type distillation schizolysis integration equipment.
Background
The existing cracking equipment is basically divided into two types, one type is intermittent cracking, and the other type is continuous cracking, and the existing technology has the defects that: although batch cracking equipment is mature, the batch cracking equipment is lack of continuity, the automation control level of the equipment is low, more labor is needed, the labor cost is increased, the production efficiency is low, the production process needs to be continuously heated and cooled, the equipment is greatly damaged, the production process is unstable, the solid carbon black and distillation are respectively operated in the production process, the danger coefficient is large, and the pollution of solid carbon black particles is large.
At present, manufacturers for producing continuous equipment in China are basically zero, and only stay in a conceptual stage if any, a prototype cannot realize continuous production, the stability is poor, the treatment capacity does not meet the theoretical requirement, and the invention mainly solves the primary technical problems of the continuity and the stability of cracking equipment. And the integration of cracking and distillation is realized.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome not enough among the prior art, provide a continuous type distillation schizolysis integration equipment, can effectually slow down the speed that the motor heaied up, improved the durability of motor.
The utility model discloses a realize through following technical scheme: the utility model provides a continuous type distillation schizolysis integration equipment, is including the charge-in system that connects gradually, the schizolysis system, oil gas cooling system, circulating water cooling system, still be connected with ejection of compact system and gas cleaning system in the schizolysis system, circulating water cooling system still is connected with noncondensable combustible gas clean system, its characterized in that: the feeding system comprises a feeding bin, and a conveying pipe is connected to the feeding bin; the cracking system comprises a cracker, wherein the cracker is connected with a continuous heat supply device and is connected with the other end of the conveying pipe; the oil-gas cooling system comprises an oil separator connected with the cracker, and the oil separator is also connected with a cooler; the flue gas purification system comprises a flue condenser connected with the distillation reaction kettle, the output end of the flue condenser is connected with an induced draft fan, the output end of the induced draft fan is connected with an atomizing tower, and a chimney is connected to the atomizing tower; the discharge gate department of the cooler of telling is connected with middle oil tank, still be connected with noncondensable combustible gas clean system on the middle oil tank, noncondensable combustible gas clean system includes noncondensable combustible gas purifier and combustible gas discharging device.
Further, the combustible gas discharging device is also connected with the continuous heating device.
Further, flue gas purification system includes the deposit box, the lateral wall of deposit box sails upward and is provided with sewage entry and outlet, it is provided with the filler opening to be close to sewage entry one side on the deposit box, still be provided with filter equipment and peculiar smell remove device in the deposit box, UV photodissociation machine can be chooseed for use to the peculiar smell remove device.
Further, feed system includes horizontal screw feeder I, screw feeder's end-to-end connection has the vertical screw feeder II of perpendicular to screw feeder I, screw feeder III of perpendicular to screw feeder II is connected to screw feeder II's end-to-end connection, and screw feeder II's end still is provided with the ball-valve.
Further, circulating water cooling system includes the cooling tower, be connected with the condenser on the cooling tower, be connected with the holding vessel in advance on the condenser, the holding vessel still is connected with the cooling tower through the condenser pipe in advance.
The beneficial effects of the utility model reside in that:
1. the utility model discloses can realize the production of schizolysis distillation plant continuity integration, save manufacturing cost, increase production efficiency to the security improves greatly.
2, the utility model discloses compare more original equipment and reduce heating system, through oil water separator, the condensation gas etc. has realized the waste gas utilization, has reduced the pollution to the environment, has improved material utilization and has rateed, has reduced the pollution to the environment.
Drawings
Fig. 1 is a schematic connection diagram of embodiment 1 of the present invention;
FIG. 2 is a schematic view of the connection of the feeding system of example 1 of the present invention;
fig. 3 is a schematic connection diagram of a circulating water cooling system according to embodiment 1 of the present invention;
FIG. 4 is a schematic view of a sewage purification apparatus according to embodiment 1 of the present invention;
wherein: 1-cracker, 2-feeding system, 3-spiral slag extractor, 4-slag oil tank, 5-deposition tank, 51-water outlet, 52-filtering device, 53-peculiar smell removing device, 56-filling port, 57-sewage inlet, 6-slag discharging device, 7-air bag, 8-condensing pipe, 9-prestorage tank, 10-condenser, 12-oil-water separator, 13-oil storage tank, 14-sewage purifying device, 15-adsorption tank, 16-flue condenser, 17-spray tower, 18-adsorption tower, 19-chimney, 20-cooling tower, 21-feed hopper, 22-spiral feeder I, 23-spiral feeder II, 24-ball valve and 25-spiral feeder III.
Detailed Description
In the description of the present invention, it should also be noted that, unless otherwise explicitly specified or limited, the terms "disposed," "mounted," "connected," and "connected" are to be construed broadly, e.g., as meaning either a fixed connection, a removable connection, or an integral connection; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Example 1
The continuous distillation and cracking integrated equipment comprises a feeding system 2, a cracking system, an oil cooling system and a circulating water cooling system which are sequentially connected, wherein the cracking system is further connected with a discharging system and a flue gas purification system, the circulating water cooling system is connected with a non-condensable combustible gas purification system, the feeding system 2 comprises a material conveying device, the material conveying device comprises a horizontal spiral feeder I, a feeding bin is machined on the spiral feeder I, the tail end of the spiral feeder I is connected with a vertical spiral feeder II perpendicular to the spiral feeder I, the tail end of the spiral feeder II is connected with a spiral feeder III perpendicular to the spiral feeder II, and the tail end of the spiral feeder II is further provided with a ball valve; the cracking system comprises a cracker 1, a continuous heat supply device is connected to the cracker 1, and the cracker 1 is connected with the other end of the screw feeder III; the cracker 1 is also connected with a spiral slag discharging machine 3, the output end of the spiral slag discharging machine 3 is connected with a slag discharging device 6, the oil-gas cooling system comprises an oil-gas bag 7 which is connected with the cracker 1 and used for collecting oil gas, the oil-gas bag 7 is connected with a condensing pipe 8 and a residual oil tank 4, the oil gas is liquefied in the condensing pipe 8, the condensing pipe 8 is connected with a pre-storage tank 9, liquid oil in the pre-storage tank 9 enters an oil-water separator 12 through water seal, and the oil-water separator 12 is connected with an oil storage tank 13; the flue gas purification system comprises a flue condenser 16 connected with the cracker 1, the output end of the flue condenser 16 is connected with a spray tower 17, the output end of the spray tower 17 is connected with an adsorption tower 18, and the adsorption tower 18 is connected with a chimney 19; the circulating water cooling system comprises a cooling tower 20 connected with a flue condenser, the cooling tower 20 is connected with a condenser 10, the condenser 10 is connected with a pre-storage tank 9, and the pre-storage tank 9 is also connected with the cooling tower 20 through a condensing pipe 8; it still is connected with noncondensable combustible gas clean system on the prestorage tank 9, noncondensable combustible gas clean system includes oil water separator 12, be connected with oil storage tank 13 and sewage purification device 14 on the oil water separator 12, still be connected with adsorption tank 15 on the sewage purification device 14, sewage purification device 14 includes deposition case 5, be provided with sewage entry and outlet on the lateral wall of deposition case 5, be provided with the filler opening near sewage entry one side on the deposition case, still be provided with filter equipment and peculiar smell remove device in the deposition case, UV photodissociation machine can be chooseed for use to the peculiar smell remove device, combustible gas discharge device still links to each other with continuous heating device, can let in continuous heating device with waste gas like this and burn the release energy, thereby increase the utilization efficiency of material.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications and variations can be made in the embodiments or in part of the technical features of the embodiments without departing from the spirit and the scope of the invention.
Claims (5)
1. The utility model provides a continuous type distillation schizolysis integration equipment, is including the charge-in system that connects gradually, the schizolysis system, oil gas cooling system, circulating water cooling system, the schizolysis system still is connected with discharge system and gas cleaning system, circulating water cooling system still is connected with noncondensable combustible gas clean system, its characterized in that: the feeding system comprises a feeding bin, and a material conveying device is connected to the feeding bin; the cracking system comprises a cracker, wherein the cracker is connected with a continuous heat supply device and is connected with a material conveying device; the oil-gas cooling system comprises an oil separator connected with the cracker, and the oil separator is also connected with a cooler; the flue gas purification system comprises a flue condenser connected with the cracker, the output end of the flue condenser is connected with a spray tower, the spray tower is connected with an adsorption tower, and the adsorption tower is connected with a chimney; the circulating water cooling system comprises a cooling tower connected with a flue condenser, the cooling tower is connected with a condenser, the condenser is connected with a pre-storage tank, and the pre-storage tank is also connected with a non-condensable combustible gas purification system; the non-condensable combustible gas purification system comprises an oil-water separator connected with a pre-storage tank, the oil-water separator is connected with an oil storage tank and a sewage purification device, and the sewage purification device is connected with an adsorption tank.
2. The integrated continuous distillation and cracking equipment as claimed in claim 1, wherein: the combustible gas discharge device is also connected with the continuous heating device.
3. The integrated continuous distillation and cracking equipment as claimed in claim 1, wherein: sewage purification device, including the deposit case, the lateral wall of deposit case sails upward and is provided with sewage entry and outlet, it is provided with the filler opening to be close to sewage entry one side on the deposit case, still be provided with filter equipment and peculiar smell remove device in the deposit case, UV photodissociation machine can be chooseed for use to the peculiar smell remove device.
4. The integrated continuous distillation and cracking equipment as claimed in claim 1, wherein: the feeding system comprises a horizontal screw feeder I, the tail end of the screw feeder is connected with a vertical screw feeder II perpendicular to the screw feeder I, the tail end of the screw feeder II is connected with a screw feeder III perpendicular to the screw feeder II, and the tail end of the screw feeder II is further provided with a ball valve.
5. The integrated continuous distillation and cracking equipment as claimed in claim 1, wherein: the circulating water cooling system comprises a cooling tower, a condenser is connected to the cooling tower, a pre-storage tank is connected to the condenser, and the pre-storage tank is further connected with the cooling tower through a condensation pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920447070.XU CN209816030U (en) | 2019-04-03 | 2019-04-03 | Continuous distillation and cracking integrated equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920447070.XU CN209816030U (en) | 2019-04-03 | 2019-04-03 | Continuous distillation and cracking integrated equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209816030U true CN209816030U (en) | 2019-12-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920447070.XU Active CN209816030U (en) | 2019-04-03 | 2019-04-03 | Continuous distillation and cracking integrated equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209816030U (en) |
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2019
- 2019-04-03 CN CN201920447070.XU patent/CN209816030U/en active Active
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