CN214813525U

CN214813525U - Emulsion oil residue heating device

Info

Publication number: CN214813525U
Application number: CN202023107750.9U
Authority: CN
Inventors: 许世军; 杨先林; 马祖兵; 任明军; 毛爽; 冯建华; 胡传兵
Original assignee: Sichuan Mianzhu Chuanrun Chemical Co ltd; Sichuan Hongda Co ltd
Current assignee: Sichuan Mianzhu Chuanrun Chemical Co ltd; Sichuan Hongda Co ltd
Priority date: 2020-12-22
Filing date: 2020-12-22
Publication date: 2021-11-23
Anticipated expiration: 2030-12-22

Abstract

The utility model discloses an emulsified oil residue heating device, which belongs to the technical field of oil residue treatment devices after emulsified water treatment in the chemical field; the device comprises a base, wherein at least one heating layer with an oil residue placing groove is arranged on the base, the heating layer comprises a storage box with the oil residue placing groove and a heating device arranged below the storage box, a liquid outlet is formed in one end part of the storage box, and produced oil water can be discharged through the liquid outlet for collection after the oil residue is placed on the storage box for heating; the utility model provides an among the traditional chemical industry the dregs of fat that produce in the emulsified water treatment process of oil-water mixture is of high quality, and the processing cost is high, and the problem of oil recovery efficiency is with the help of the effectual evaporation of water that can make in the dregs of fat of steam heating's mode, and moisture is at the in-process of evaporation, and the effectual oil with in the dregs of fat also takes out, realizes the further collection to oil.

Description

Emulsion oil residue heating device

Technical Field

The utility model relates to an emulsion dregs of fat heating device belongs to the dregs of fat processing apparatus technical field after synthetic ammonia chemical industry field emulsified water handles.

Background

The oil-water separation is mainly based on the density difference or chemical property difference of water and oil, and utilizes gravity settling principle or other physical and chemical reaction to remove impurities or complete the separation of oil and water.

In the chemical field, water cooling is usually adopted, and the used waste water is often accompanied with certain oil, and most of the oil can be separated after standing. However, this physical method can only extract most of the oil, and the remaining waste water contains a large amount of oil, so that the separated water cannot be recycled, and the utilization rate thereof is very low, and thus water cannot be efficiently recovered. In general, the oil is generally chemically treated by means of emulsification and then separated, which allows efficient extraction of the water and is reused, for example: synthetic ammonia or cooling.

Based on the above specific process, a certain amount of chemical waste oil residues are generated after treatment, and in the treatment of the waste oil residues, the treatment is usually outsourcing treatment, and the price of the outsourcing treatment is relatively expensive, while in the specific operation, the reduction of the cost of waste treatment is to reduce the water content and the oil content of non-oil residues, thereby realizing the reduction of the whole cost.

Disclosure of Invention

The invention of the utility model aims to: aiming at the existing problems, the emulsified oil residue heating device is provided, the weight of the oil residue generated after the emulsified water is treated can be effectively reduced, so that the oil recovery is effectively improved, the treatment cost of waste residues is reduced, the device is more environment-friendly, and the cost consumption of the whole process is reduced.

The utility model adopts the technical scheme as follows:

the utility model provides an emulsion dregs of fat heating device, includes the base, sets up the zone of heating that the one deck has the dregs of fat standing groove on this base at least, and this zone of heating is including the storage box that has the dregs of fat standing groove and set up the heating device in storage box below, and a tip of this storage box is provided with the leakage fluid dram, and after placing the dregs of fat on the storage box and heating, the profit accessible leakage fluid dram discharge of output is collected.

Further, be provided with 2 layers of zone of heating that have the dregs of fat standing groove on this base, including first zone of heating and second zone of heating, the zone of heating on this 2 layers sets up for from top to bottom.

Further, the heating device is a steam U-shaped coil, or/and the heating device comprises a steam U-shaped coil and a shell, and the steam U-shaped coil is arranged in the shell.

Furthermore, the steam outlet of the steam U-shaped coil pipe of the first heating layer is communicated with the air inlet of the steam U-shaped coil pipe of the second heating layer so as to realize the full utilization of the waste heat of the steam.

Furthermore, a first liquid discharge port is arranged on the storage box with the first heating layer, a second liquid discharge port is arranged on the storage box with the second heating layer, and the first liquid discharge port is positioned above the storage box with the second heating layer.

Further, the first liquid discharge port and the second liquid discharge port are respectively located at two end portions in the length direction of the heating layer for increasing the path of the liquid.

Further, the bottom of the storage box of the first heating layer is an inclined plane.

Furthermore, one side of the bottom of the storage box on the first heating layer where the first liquid discharge port is located is lower than the other side of the bottom of the storage box on the first heating layer.

Furthermore, the bottom of the storage box of the second heating layer is an inclined plane.

Furthermore, one side of the bottom of the storage box on the second heating layer where the second liquid outlet is located is lower than the other side of the bottom of the storage box on the second heating layer.

To sum up, owing to adopted above-mentioned technical scheme, the beneficial effects of the utility model are that:

the utility model discloses an emulsion dregs of fat heating device has solved the dregs of fat that produces in the emulsification water treatment process of oil water mixture among the traditional chemical industry, and the processing cost is high, the problem of oil recovery efficiency, the effectual evaporation of water that can make in the dregs of fat with the help of steam heating's mode, moisture is at the in-process of evaporation, the effectual oil with in the dregs of fat also takes out, realize the further collection to oil, and simultaneously, the steam that produces in the heating mode that utilizes steam can effectual realization with the help of the chemical industry technology, thereby effectively improve the utilization ratio of energy.

Drawings

Fig. 1 is a schematic structural diagram of the present invention;

fig. 2 is a schematic diagram of the structure of the steam coil.

The labels in the figure are: 1-a base, 2-a heating layer, 21-a first heating layer, 22-a second heating layer, 3-a storage box, 4-a heating device, 51-a first liquid discharge port and 52-a second liquid discharge port.

Detailed Description

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

In order to make the objects, technical solutions and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.

Examples

The utility model provides an emulsion dregs of fat heating device, as shown in fig. 1 and 2, includes base 1, sets up the zone of heating 2 that the one deck has the dregs of fat standing groove on this base 1 at least, and this zone of heating is including the storage box 3 that has the dregs of fat standing groove and set up in heating device 4 of storage box below, and one end of this storage box 3 is provided with the leakage fluid dram, places the dregs of fat on the storage box through heating, and the profit accessible leakage fluid dram of output is discharged and is collected.

In this embodiment, with the help of the effectual moisture evaporation that can make in the dregs of fat of heating, moisture is at the in-process of evaporation, and the effectual oil with in the dregs of fat also takes out, realizes the further collection to oil, simultaneously, the heating methods that utilizes steam can effectually realize with the help of the steam that produces in the chemical industry technology to effectively improve the utilization ratio of energy.

In the traditional process, the produced oil and water are generally demulsified and separated from each other, the separated oil residue needs to be subjected to outsourcing treatment based on the requirements of environmental protection and hazardous waste treatment, a weight charging mode is generally adopted during the outsourcing treatment, the water content and the oil content of the discharged oil residue are generally higher, and the cost is higher when the outsourcing treatment is carried out together, so the weight of the whole oil residue can be effectively reduced by adopting the design in the embodiment. In addition, the collected oil can be recycled again to be used as a chemical raw material for producing similar lipid products, so that the oil can be recycled.

Based on the design basis of above-mentioned concrete structure, as further design, be provided with 2 layers of zone of heating 2 that have the dregs of fat standing groove on this base 1, including first zone of heating 21 and second zone of heating 22, the zone of heating on this 2 layers is setting up from top to bottom. Due to the specific design, a better heating effect can be realized, and the water evaporation efficiency is effectively improved. Specifically, the first heating layer 21 and the second heating layer 22 are welded by using a connecting member to form an upper-lower layer structure.

More specifically, the base is provided with 4 supporting legs, so that the device can be installed.

Based on the above specific structure, as a more specific design, the heating device 22 is a steam U-shaped coil, or/and the heating device 22 includes a steam U-shaped coil and a housing, and the steam U-shaped coil is disposed in the housing. As a specific description, the heating device below the first heating layer 21 includes a steam U-shaped coil disposed inside a housing, and the housing. As a specific example, the integration of the steam U-coil into the housing is a common practice in the art and is not specifically shown, but its primary purpose is to have better uniformity of heating. More specifically, the heating device below the second heating layer 22 is a steam U-shaped coil.

On the basis of the design of above-mentioned specific structure, as more specific design, the steam outlet of the steam U-shaped coil pipe of this first zone of heating communicates with the air inlet of the steam U-shaped coil pipe of second zone of heating in order to realize the waste heat make full use of steam. The mode connects the upper and lower heaters in series to realize the full application of the whole device to heat energy. As a general knowledge, a steam U-coil is one having an inlet end and an outlet end for steam. As a specific description, the steam inlet of the heating device below the first heating layer 21 is used as a total steam inlet, the steam outlet of the heating device below the second heating layer 22 is used as a total steam outlet, a water condensation liquid collecting box can be arranged at the total steam outlet, and the residual steam can be directly discharged.

On the basis of the above specific structure, as a more specific design, a first drain port 51 is provided on the storage box of the first heating layer 21, a second drain port 52 is provided on the storage box of the second heating layer 22, and the first drain port 51 is located above the storage box of the second heating layer 22. More specifically, the liquid discharged from the first liquid discharge port may directly drip into the storage box of the second heating layer.

As a more specific design, the first drain port 51 and the second drain port 52 are located at both ends in the heating layer longitudinal direction, respectively, for increasing the path of the liquid. The design can effectively increase the flow of the oil, and is more favorable for the evaporation of water in the oil in the whole process, so that the purity of the oil is higher, and the oil is more convenient to use.

Based on the design basis of the above specific structure, as a more specific design, the bottom of the storage box of the first heating layer 21 is an inclined surface.

Due to the design of the inclined surface, as a more specific design, the bottom side of the storage box of the first heating layer where the first liquid discharge port 51 is located is lower than the bottom side of the storage box of the first heating layer. The design of this mode is favorable to the collection of oil, and under oil self action of gravity, oil can be automatic to the play gathering of leakage fluid dram to can the effectual recovery that realizes oil.

As a similar design, in particular, the bottom of the second heating layer 22 is sloped.

More specifically, the bottom side of the storage box of the second heating layer where the second liquid outlet 52 is located is lower than the bottom side of the storage box of the second heating layer.

On the basis of the design of the specific structure, in order to ensure the purity of the collected oil, a filter screen is arranged at the first liquid discharge port or/and the second liquid discharge port. Impurities in the oil can be effectively reduced through the filter screen.

To sum up, the utility model discloses an emulsion dregs of fat heating device has solved the dregs of fat quality that produces among the traditional chemical industry in the emulsification water treatment process of oil-water mixture, and the processing cost is high, the problem of oil recovery efficiency, with the help of the effectual evaporation of water that can make in the dregs of fat of steam heating's mode, moisture is at the in-process of evaporation, and the effectual oil with in the dregs of fat also takes away, realizes the further collection to oil, and simultaneously, the heating mode that utilizes steam can effectual realization be with the help of the steam that produces in the chemical industry technology to effectively improve the utilization ratio of energy.

The above description is only exemplary of the present invention and should not be taken as limiting the scope of the present invention, as any modifications, equivalents, improvements and the like made within the spirit and principles of the present invention are intended to be included within the scope of the present invention.

Claims

1. The emulsion oil residue heating device is characterized in that: including base (1), set up one deck at least on this base (1) and have zone of heating (2) of oil residue standing groove, this zone of heating is including storage box (3) that have the oil residue standing groove and set up in heating device (4) of storage box below, and a tip of this storage box (3) is provided with the leakage fluid dram, places the oil residue on the storage box and heats the back, and the profit accessible leakage fluid dram of output is discharged and is collected.

2. The apparatus for heating emulsified oil residues as set forth in claim 1, wherein: be provided with 2 layers on this base (1) and have zone of heating (2) of dregs of fat standing groove, including first zone of heating (21) and second zone of heating (22), the zone of heating on this 2 layers is setting up from top to bottom.

3. The apparatus for heating emulsified oil residues as set forth in claim 2, wherein: the heating device (4) is a steam U-shaped coil pipe, or/and the heating device (4) comprises a steam U-shaped coil pipe and a shell, and the steam U-shaped coil pipe is arranged in the shell.

4. The apparatus for heating emulsified oil residues as set forth in claim 3, wherein: the steam outlet of the steam U-shaped coil pipe of the first heating layer is communicated with the air inlet of the steam U-shaped coil pipe of the second heating layer so as to realize the full utilization of the waste heat of the steam.

5. The apparatus for heating emulsified oil residues as set forth in claim 2, wherein: a first liquid outlet (51) is arranged on the storage box of the first heating layer (21), a second liquid outlet (52) is arranged on the storage box of the second heating layer (22), and the first liquid outlet (51) is positioned above the storage box of the second heating layer (22).

6. The apparatus for heating emulsified oil residues as set forth in claim 5, wherein: the first liquid discharge port (51) and the second liquid discharge port (52) are respectively positioned at two ends of the heating layer in the length direction for increasing the liquid path.

7. The apparatus for heating emulsified oil residues as set forth in claim 5, wherein: the bottom of the storage box of the first heating layer (21) is an inclined plane.

8. The apparatus for heating emulsified oil residues as set forth in claim 7, wherein: one side of the bottom of the storage box of the first heating layer where the first liquid discharge port (51) is located is lower than the other side of the bottom of the storage box of the first heating layer.

9. The apparatus for heating emulsified oil residues as set forth in claim 5, wherein: the bottom of the storage box of the second heating layer (22) is an inclined plane.

10. The apparatus for heating emulsified oil residues as set forth in claim 9, wherein: the bottom side of the storage box of the second heating layer where the second liquid outlet (52) is positioned is lower than the other side of the bottom of the storage box of the second heating layer.