Bisphenol A dust recycling device

By designing a bisphenol A dust recycling device, the risk of excessive dust and electrostatic explosion during the unpacking and feeding of bisphenol A is solved, effective dust recovery and nitrogen recycling are achieved, and material loss and use costs are reduced.

CN222856255UActive Publication Date: 2025-05-13HUBEI GANNING PETROCHEMICAL NEW MATERIALS CO LTD
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Patent Information

Application Number
CN202421708137.8
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-07-18
Publication Date
2025-05-13
Estimated Expiration
2034-07-18

AI Technical Summary

Technical Problem

During the unpacking and feeding process, bisphenol A will produce a large amount of dust, causing large material loss, and there is a risk of static electricity aggregation and explosion, endangering personnel safety.

Method used

A bisphenol A dust recycling device is designed, including a bisphenol A dust collector, a dust collection tank, a nitrogen recovery dust collector and a compressor. The dust is recovered through a dust collector and a circulating air duct system, and nitrogen is used for recycling.

Benefits of technology

It effectively reduces dust during the bisphenol A feeding process, reduces the risk of material loss and electrostatic explosion, and at the same time realizes the recycling of nitrogen, reducing the cost of use.

✦ Generated by Eureka AI based on patent content.

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Abstract

A bisphenol A dust recycling device comprises a bisphenol A dust remover, the bisphenol A dust remover is communicated with a feeding pipe and provided with a dust removing fan, a discharging port in the lower end of the bisphenol A dust remover is communicated with a dust collecting tank through a first discharging pipe, a discharging port of the dust collecting tank is communicated with a bisphenol A stock bin through a second discharging pipe, and a nitrogen recycling dust remover is installed on the bisphenol A stock bin. The nitrogen recovery dust remover is communicated with the dust collecting tank through a circulating gas pipe; and a compressor is mounted on the circulating gas pipe. The utility model is used for solving the problems of large loss of bisphenol A materials and risk of casualties caused by dust explosion due to electrostatic aggregation.
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Description

Technical Field

[0001] The utility model relates to the technical field of dust recovery, in particular to a bisphenol A dust recovery and utilization device. Background Art

[0002] The ester exchange method of polycarbonate synthesis polymerization generally uses bisphenol A and diphenyl carbonate as polymerization raw materials. Since bisphenol A is packaged in ton bags, it needs to be unpacked and fed into the materials before use. During the unpacking and feeding process of bisphenol A, a large amount of dust will appear, the bisphenol A material will be damaged, and there is a risk of static electricity accumulation and dust explosion leading to casualties. Summary of the invention

[0003] The technical problem to be solved by the utility model is to provide a bisphenol A dust recovery and utilization device for solving the problems of large bisphenol A material loss and the risk of casualties caused by explosion of electrostatically accumulated dust.

[0004] In order to solve the above problems, the technical solution of the utility model is:

[0005] A bisphenol A dust recovery and utilization device comprises a bisphenol A dust collector, the bisphenol A dust collector is connected with a feed pipe and a dust removal fan, a discharge port at the lower end of the bisphenol A dust collector is connected with a dust collection tank through a first discharge pipe, a discharge port of the dust collection tank is connected with a bisphenol A silo through a second discharge pipe, a nitrogen recovery dust collector is installed on the bisphenol A silo, the nitrogen recovery dust collector is connected with the dust collection tank through a circulating air pipe, and a compressor is installed on the circulating air pipe.

[0006] It also includes a nitrogen gas cabinet, which is connected to the nitrogen recovery dust collector.

[0007] A cut-off valve is installed on the first discharge pipe.

[0008] A material level meter is provided in the bisphenol A dust collector.

[0009] A compressed nitrogen valve is installed on the circulating gas pipe.

[0010] The beneficial effects of the utility model are:

[0011] 1. It can recycle bisphenol A dust, reduce dust in the process of bisphenol A feeding, and reduce the loss of bisphenol A materials.

[0012] 2. Reduce the risk of dust explosion caused by static electricity accumulation during the feeding process of bisphenol A.

[0013] 3. Nitrogen can be recycled for reuse, reducing the cost of nitrogen use. BRIEF DESCRIPTION OF THE DRAWINGS

[0014] The present invention will be further described below in conjunction with the accompanying drawings:

[0015] Figure 1 It is a structural schematic diagram of the utility model.

[0016] In the figure: nitrogen compressor 1, nitrogen gas cabinet 2, nitrogen recovery dust collector 3, bisphenol A silo 4, dust removal fan 5, bisphenol A dust collector 6, level meter 7, shut-off valve 8, dust collection tank 9, compressed nitrogen valve 10. DETAILED DESCRIPTION

[0017] like Figure 1 A bisphenol A dust recovery and utilization device includes a bisphenol A dust collector 6, which is connected to a feed pipe and a dust removal fan 5, the lower end discharge port of the bisphenol A dust collector 6 is connected to a dust collection tank 9 through a first discharge pipe, and the discharge port of the dust collection tank 9 is connected to a bisphenol A silo 4 through a second discharge pipe, and a nitrogen recovery dust collector 3 is installed on the bisphenol A silo 4, and the nitrogen recovery dust collector 3 is connected to the dust collection tank through a circulating air pipe, and a compressor 1 is installed on the circulating air pipe. It also includes a nitrogen gas cabinet 2, which is connected to the nitrogen recovery dust collector 3. A shut-off valve 8 is installed on the first discharge pipe. A material level meter 7 is provided on the bisphenol A dust collector 6. A compressed nitrogen valve 10 is installed on the circulating air pipe.

[0018] The working process of the utility model is as follows: bisphenol A dust is fed into the bisphenol A dust collector 6 through the feed pipe for recovery. After the material level meter 7 detects that the bisphenol A dust collector 6 has accumulated to a certain material level, the shut-off valve 8 is opened, and the dust in the bisphenol A dust collector 6 falls into the dust collecting tank 9. After the dust discharge is completed, the shut-off valve 8 is closed, the nitrogen compressor 1 is started, and the compressed nitrogen valve 10 is opened to fluidize the dust in the dust collecting tank 9 and send it to the bisphenol A silo 4 for production use. The nitrogen returns to the nitrogen gas cabinet 2 through the bisphenol A silo 4 and the nitrogen recovery dust collector 3, and the nitrogen gas cabinet 2 is recycled through the nitrogen compressor 1.

[0019] The above embodiments are only preferred technical solutions of the present invention and should not be regarded as limitations of the present invention. The protection scope of the present invention shall be the technical solutions recorded in the claims, including equivalent replacement solutions of the technical features in the technical solutions recorded in the claims. That is, equivalent replacement improvements within this scope are also within the protection scope of the present invention.

Claims

1. A bisphenol A dust recovery and utilization device, characterized in that: The invention comprises a bisphenol A dust collector (6), the bisphenol A dust collector (6) is connected to a feed pipe and is equipped with a dust removal fan (5), the lower end discharge port of the bisphenol A dust collector (6) is connected to a dust collection tank (9) through a first discharge pipe, the discharge port of the dust collection tank (9) is connected to a bisphenol A silo (4) through a second discharge pipe, a nitrogen recovery dust collector (3) is installed on the bisphenol A silo (4), the nitrogen recovery dust collector (3) is connected to the dust collection tank (9) through a circulating air pipe, and a compressor (1) is installed on the circulating air pipe.

2. The bisphenol A dust recovery and utilization device according to claim 1, characterized in that: It also includes a nitrogen gas cabinet (2), which is connected to a nitrogen recovery dust collector (3).

3. The bisphenol A dust recovery and utilization device according to claim 1, characterized in that: A shut-off valve (8) is installed on the first discharge pipe.

4. The bisphenol A dust recovery and utilization device according to claim 1, characterized in that: The bisphenol A dust collector (6) is provided with a material level meter (7).

5. The bisphenol A dust recovery and utilization device according to claim 1, characterized in that: A compressed nitrogen valve (10) is installed on the circulating gas pipe.