CN210237544U - Oil residue treatment system - Google Patents
Oil residue treatment system Download PDFInfo
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- CN210237544U CN210237544U CN201921291794.6U CN201921291794U CN210237544U CN 210237544 U CN210237544 U CN 210237544U CN 201921291794 U CN201921291794 U CN 201921291794U CN 210237544 U CN210237544 U CN 210237544U
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- slag
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Abstract
The utility model provides an oil residue treatment system, which comprises a residue wax constant temperature tank, a residue wax buffer tank, a pre-coating tank and a filter; the periphery of the slag wax constant-temperature tank is provided with a constant-temperature tank heat tracing; the slag wax constant temperature tank is provided with a bottom discharge port and a middle discharge port, the slag wax buffer tank is provided with a bottom discharge port and a middle discharge port, and the middle discharge port of the slag wax constant temperature tank is communicated with the middle discharge port of the slag wax buffer tank; the feed inlet of the pre-coating tank is communicated with the middle discharge port of the slag wax constant-temperature tank and the middle discharge port of the slag wax buffer tank through a tee; and the discharge hole of the pre-coating tank is communicated with the feed inlet of the filter. The utility model discloses utilize sediment wax constant temperature jar and sediment wax buffer tank to stew the layering earlier with the sediment wax, sink the heavy component in the sediment wax naturally, discharge from the bottom, as the raw materials of coating, the lower light liquid of ash content that the middle part was adopted is sent to the filter, adopts a small amount of filter aid can obtain the oil that colourity and sediment content meet the standard.
Description
Technical Field
The utility model belongs to the technical field of the coal chemical industry, especially, relate to an oil residue processing system.
Background
Because the residue discharged from the reactor contains a large amount of oil and iron catalysts, the conventional treatment process needs to enter a precoated filtering system for treatment through reasonably proportioning filter aids, the treated residue needs to contain a certain oil content according to the characteristics of the residue, so that the catalysts are in a wrapped state, otherwise, fire accidents are easily caused, the residue needs to be sent to dangerous waste for incineration and then buried for treatment, thus, the consumption of treatment additives is large, the treatment cost of the dangerous waste is extremely high, the treatment investment is huge, and the huge waste is caused.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an oil residue processing system, the utility model provides an oil residue processing system can practice thrift a large amount of auxiliaries, and changing waste into valuables has improved the economic benefits of device simultaneously.
The utility model provides an oil residue treatment system, which is characterized by comprising a residue wax constant temperature tank, a residue wax buffer tank, a pre-coating tank and a filter;
the periphery of the slag wax constant-temperature tank is provided with a constant-temperature tank heat tracing;
the slag wax constant temperature tank is provided with a bottom discharge port and a middle discharge port, the slag wax buffer tank is provided with a bottom discharge port and a middle discharge port, and the middle discharge port of the slag wax constant temperature tank is communicated with the middle discharge port of the slag wax buffer tank;
the feed inlet of the pre-coating tank is communicated with the middle discharge port of the slag wax constant-temperature tank and the middle discharge port of the slag wax buffer tank through a tee;
and the discharge hole of the pre-coating tank is communicated with the feed inlet of the filter.
Preferably, the filter is also provided with a second feeding hole, and the second feeding hole is communicated with a middle discharge hole of the slag wax constant-temperature tank and a middle discharge hole of the slag wax buffer tank.
Preferably, the middle discharge port of the slag wax constant-temperature tank and the middle discharge port of the slag wax buffer tank are positioned at the same horizontal height.
Preferably, a precoating filter screen is arranged in the filter.
The utility model provides an oil residue treatment system, which comprises a residue wax constant temperature tank, a residue wax buffer tank, a pre-coating tank and a filter; the periphery of the slag wax constant-temperature tank is provided with a constant-temperature tank heat tracing; the slag wax constant temperature tank is provided with a bottom discharge port and a middle discharge port, the slag wax buffer tank is provided with a bottom discharge port and a middle discharge port, and the middle discharge port of the slag wax constant temperature tank is communicated with the middle discharge port of the slag wax buffer tank; the feed inlet of the pre-coating tank is communicated with the middle discharge port of the slag wax constant-temperature tank and the middle discharge port of the slag wax buffer tank through a tee; and the discharge hole of the pre-coating tank is communicated with the feed inlet of the filter. The utility model discloses utilize sediment wax constant temperature jar and sediment wax buffer tank to stew the layering earlier with the sediment wax, sink the heavy component in the sediment wax naturally, discharge from the bottom, as the raw materials of coating, the lower light liquid of ash content that the middle part was adopted is sent to pot and filter of precoating, adopts a small amount of filter aid can obtain the oil that colourity and sediment content meet the standard.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required to be used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the provided drawings without creative efforts.
FIG. 1 is a schematic view of the medium wax processing system of the present invention,
wherein, 1 is a slag wax constant temperature tank, 2 is a slag wax buffer tank, 3 is a pre-coating tank, and 4 is a filter.
Detailed Description
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.
The utility model provides an oil residue treatment system, the structure of which is shown in figure 1, comprising a residue wax constant temperature tank, a residue wax buffer tank, a pre-coating tank and a filter;
the periphery of the slag wax constant-temperature tank is provided with a constant-temperature tank heat tracing;
the slag wax constant temperature tank is provided with a bottom discharge port and a middle discharge port, the slag wax buffer tank is provided with a bottom discharge port and a middle discharge port, and the middle discharge port of the slag wax constant temperature tank is communicated with the middle discharge port of the slag wax buffer tank;
the feed inlet of the pre-coating tank is communicated with the middle discharge port of the slag wax constant-temperature tank and the middle discharge port of the slag wax buffer tank through a tee;
and the discharge hole of the pre-coating tank is communicated with the feed inlet of the filter.
The utility model discloses in, be provided with around the sediment wax constant temperature jar and accompany the heat facility for the sediment wax that keeps in the sediment wax constant temperature jar keeps at appropriate temperature, prevents that the sediment wax from solidifying. And a discharge hole is formed in the bottom of the wax residue constant temperature tank and used for discharging heavy components in the wax residue deposited at the bottom of the wax residue constant temperature tank. And a middle discharge hole is formed in the middle of the slag wax constant-temperature tank and used for outputting light liquid in the slag wax with lower ash content in the middle of the tank.
And a discharge hole is formed in the bottom of the slag wax constant-temperature tank and used for discharging heavy components in the slag wax deposited at the bottom of the slag wax buffer tank. And a middle discharge hole is formed in the middle of the slag wax buffer tank and used for outputting light liquid in the slag wax with lower ash content in the middle of the tank.
The utility model discloses in, the middle part discharge gate of sediment wax constant temperature jar with the middle part discharge gate of sediment wax buffer tank is linked together to it is preferable on being located same level, the middle part discharge gate of sediment wax constant temperature jar still be used for with the sediment wax in the sediment wax constant temperature jar is slowly introduced except being used for containing the lower light liquid output of ash content with the middle part in the sediment wax buffer tank, realize the separation of stewing for the second time.
The feed inlet of the pre-coating tank is communicated with the middle discharge port of the slag wax constant-temperature tank and the middle discharge port of the slag wax buffer tank through a tee; a discharge port in the middle of the slag wax constant-temperature tank is connected with a feed port of the pre-coating tank and is commonly used for supplementing light liquid to the pre-coating tank;
the filter aid pre-coating device is characterized in that the pre-coating tank is provided with a filter aid feeding port for adding the filter aid into the pre-coating tank, the other feeding port of the pre-coating tank is communicated with a discharging port of the filter to realize circulation of the filter aid, a stirring device is arranged at the top of the pre-coating tank and used for mixing the filter aid with a light liquid component, the filter aid and the light liquid component are mixed in the pre-coating tank and then pumped into the filter through a pump, and the light liquid component is pumped into the filter through the pump to be filtered.
The filter is provided with two feed inlets, one feed inlet is communicated with a bottom discharge hole of the pre-coating tank and used for inputting a filter aid, the other feed inlet is communicated with a middle discharge hole of the slag wax constant-temperature tank and a middle discharge hole of the slag wax buffer tank, and a discharge hole is formed in the bottom of the filter and used for outputting qualified oil products. A filter screen and a filter disc are arranged in the filter.
The utility model discloses a system work flow as follows:
according to the characteristics of the slag wax, firstly, a constant temperature tank is adopted to keep proper constant temperature to prevent the slag wax from solidifying, then the slag wax is slowly led into a slag wax buffer tank, after standing for a certain time, heavy components in the slag wax naturally sink to the bottom of the constant temperature tank and the bottom of the buffer tank to form layers, the slag wax with high content of the heavy components is pumped out through a discharge port at the bottom of the constant temperature tank and a discharge port at the bottom of the buffer tank to serve as a raw material of the coating, light liquid with low ash content is collected at the middle part and sent into a filtering system, the light liquid is mixed with a filter aid in a pre-coating tank and then enters a filter to be filtered, and oil products with the.
Claims (4)
1. An oil residue treatment system is characterized by comprising a residue wax constant temperature tank, a residue wax buffer tank, a pre-coating tank and a filter;
the periphery of the slag wax constant-temperature tank is provided with a constant-temperature tank heat tracing;
the slag wax constant temperature tank is provided with a bottom discharge port and a middle discharge port, the slag wax buffer tank is provided with a bottom discharge port and a middle discharge port, and the middle discharge port of the slag wax constant temperature tank is communicated with the middle discharge port of the slag wax buffer tank;
the feed inlet of the pre-coating tank is communicated with the middle discharge port of the slag wax constant-temperature tank and the middle discharge port of the slag wax buffer tank through a tee;
and the discharge hole of the pre-coating tank is communicated with the feed inlet of the filter.
2. The oil residue processing system of claim 1, wherein the filter is further provided with a second feed inlet, and the second feed inlet is communicated with a middle discharge port of the residue wax constant temperature tank and a middle discharge port of the residue wax buffer tank.
3. The oil residue treatment system of claim 1, wherein the middle discharge port of the slag wax constant temperature tank and the middle discharge port of the slag wax buffer tank are located at the same horizontal height.
4. The oil residue treatment system of claim 1, wherein a filter screen and a filter disc are arranged in the filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921291794.6U CN210237544U (en) | 2019-08-09 | 2019-08-09 | Oil residue treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921291794.6U CN210237544U (en) | 2019-08-09 | 2019-08-09 | Oil residue treatment system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210237544U true CN210237544U (en) | 2020-04-03 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921291794.6U Active CN210237544U (en) | 2019-08-09 | 2019-08-09 | Oil residue treatment system |
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| Country | Link |
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| CN (1) | CN210237544U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113652261A (en) * | 2021-08-09 | 2021-11-16 | 内蒙古伊泰化工有限责任公司 | Post-treatment method of refined tail oil and refined wax |
-
2019
- 2019-08-09 CN CN201921291794.6U patent/CN210237544U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113652261A (en) * | 2021-08-09 | 2021-11-16 | 内蒙古伊泰化工有限责任公司 | Post-treatment method of refined tail oil and refined wax |
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