CN202626115U - Waste oil recycling device - Google Patents

Waste oil recycling device Download PDF

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Publication number
CN202626115U
CN202626115U CN 201220289795 CN201220289795U CN202626115U CN 202626115 U CN202626115 U CN 202626115U CN 201220289795 CN201220289795 CN 201220289795 CN 201220289795 U CN201220289795 U CN 201220289795U CN 202626115 U CN202626115 U CN 202626115U
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China
Prior art keywords
pipeline
air
product fractionation
oil product
raw material
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Expired - Lifetime
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CN 201220289795
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Chinese (zh)
Inventor
祁万仁
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Shenzhen Huayong Environmental Engineering Co ltd
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Individual
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Priority to CN 201220289795 priority Critical patent/CN202626115U/en
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Publication of CN202626115U publication Critical patent/CN202626115U/en
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Abstract

The utility model relates to a waste oil recycling device which comprises a water cycle air suction device, an air-cooled oil product fractionation device and a liquefied gas recycle and condensation compression device. The upper portion of the air-cooled oil product fractionation device is connected with the liquefied gas recycle and condensation compression device through a pipeline, and four oil recycling trays are arranged in the air-cooled oil product fractionation device. The waste oil recycling device is characterized in that the upper portion of the water cycle air suction device is connected with a raw material warming tank through a pipeline, a heating pipeline is arranged in the raw material warming tank, one end of the heating pipeline is connected with an energy saving gasification zero release boiler, ordinary pressure safety valves are installed on pipelines of the air-cooled oil product fractionation device and the liquefied gas recycle and condensation compression device, and the ordinary pressure safety valves are connected with the energy saving gasification zero release boiler through gas conveying pipelines.

Description

A kind of waste oil regeneration use device
Technical field
The utility model relates to a kind of recycling of recyclable waste device, particularly a kind of waste oil regeneration use device.
Background technology
International, domestic to various waste oil, slurry, slag, the mixed floating fluid of rubbish at present, most large enterprises such as the floating grease of water drain all take to burn, and medium-sized and small enterprises then take catalytic pyrolysis and traditional indigenous oil refining method to refine.These modes not only can cause the secondary pollution of environmental protection, also can cause the waste of renewable resources, and more fearful is cause damage for various machineries.
People begin to adopt blending method in recent years because the chemical ingredients of various waste oil is all inconsistent, the various waste oil after especially blending, though on detecting, can get by under false pretences, but it on reality is used fully and national standard very big gap is arranged.This situation is not beneficial to human consumer's rights and interests, and can disrupt the market.
Summary of the invention
The utility model is exactly a kind of waste oil regeneration use device that provides in order to overcome above-mentioned defective.
The utility model is implemented through following proposal: a kind of waste oil regeneration use device; Comprise that water cycle air extractor, air-cooled oil product fractionation plant, liquefied gas reclaim and the condensation compression set; The top of air-cooled oil product fractionation plant is reclaimed with liquefied gas through pipeline and is connected with condensing works; Inside is provided with four and receives oil tray, and the water cycle air extractor is connected with air-cooled oil product fractionation plant through pipeline, and the top of water cycle air extractor links to each other through pipeline and raw material intensification jar; The inside of raw material intensification jar is provided with the heating pipeline; And an end of heating pipeline is connected with energy-saving gasification zero release boiler, on the pipeline of air-cooled oil product fractionation plant and liquefied gas recovery and condensation compression set atmospheric relief valve is installed, and atmospheric relief valve is connected with energy-saving gasification zero release boiler through gas transmission pipeline.
The side top of said raw material intensification jar is equipped with negative pressure relief valve, and inner and upper is equipped with the receipts oil tray.
The water level limitation device is equipped with in the bottom of said air-cooled oil product fractionation plant, and is positioned at the top of the pipeline that connects the water cycle air extractor.
In the said gas transmission pipeline fireproof tempering device is installed.
The utility model less investment, be prone to be implemented safety, and is high to the comprehensive utilization ratio of various waste oil, and environmental protection and energy saving, and useless, evil material is fully used, and makes that various waste oil are slap-up to have obtained innoxious effective regeneration utilization.
Description of drawings:
Fig. 1 is the structural representation of the utility model.
Embodiment:
A kind of waste oil regeneration use device; Comprise that water cycle air extractor 1, air-cooled oil product fractionation plant 2, liquefied gas reclaim and condensation compression set 3; The top of water cycle air extractor 1 links to each other through pipeline and raw material intensification jar 6; Will be without the various waste oil of any processing: rubbish oil, tire be oily, used oil, wax oil, indigenous oil refining, sewer oil, coal tar, chemical industry oil, oil of the clear end of oil tank, slurry, slag etc. are sent into the waste oil straining installation and carried out coarse filtration; With the magazine in the waste oil, moisture separation, then filterable waste oil is irritated in 6 with being pumped into the raw material intensification, the inside of jar 6 is provided with the pipeline 6-1 that generates heat because raw material heats up; And the end of heating pipeline 6-1 is connected with energy-saving gasification zero release boiler 10; Energy-saving gasification zero release boiler 10 Heating temperatures to 110 ℃ heat up to raw material through heating pipeline 6-1 and to irritate 6 and heat up, and begin to start water cycle air extractor 1 when the temperature of irritating reaches 68 ℃ when raw material heats up; Because raw material heat up to be irritated 6 side top negative pressure relief valve 7 is installed, then effectively prevented to pump too fast and raw material heated up irritate 6 damage; Raw material then passes through the receipts oil tray 5 that 6 middle and upper parts are irritated in the raw material intensification after heating up and irritating various waste oil intensification the becoming gases in 6; Because the gas temperature that the raw material intensification is irritated in 6 is controlled at 68-86 ℃; Various waste oil in the raw material intensification filling 6 are through receipts oil tray 5 time; The gas that does not reach controlled temperature is attached to receiving on the oil tray 5; The gas that reaches controlled temperature then enters into water cycle air extractor 1 through pipeline, enters into air-cooled oil product fractionation plant 2 by the bottom of water cycle air extractor 1 and the side-lower through pipeline and air-cooled oil product fractionation plant 2 again; Be provided with water level limitation device 2-5 in the bottom of air-cooled oil product fractionation plant 2; This water level limitation device 2-5 is positioned at the top of the pipeline that connects water circle device 1; Can effectively prevent to remain waste oil and enter on the receipts oil tray 5 of air-cooled oil product fractionation plant 2, and residue waste oil is discharged through waste residue relief outlet 9; The oil product that fractionates out is upwards received on the oil tray 5 through receiving oil tray 5 and being deposited on successively; It is continuous respectively at No. 0 GB diesel fuel tank 2-4, subzero No. 10 GB diesel oil withdrawing can 2-3, kerosene withdrawing can 2-2 and No. 93 GB gasoline withdrawing can 2-1 through pipeline from top to bottom that each receives oil tray 5, makes the oil product of respectively receiving collection on the oil tray 5 enter into withdrawing can separately through pipeline; The top of air-cooled oil product fractionation plant 2 is reclaimed with liquefied gas through pipeline and is connected with condensing works 3; The gas of not received oil tray 5 absorption enters into liquefied gas through pipeline and reclaims and condensation compression set 3; Getting in the liquefied gas withdrawing can 4 through pipeline; The little of gas that does not get in liquefied gas recovery and the condensation compression set 3 then enters into gas transmission pipeline through the atmospheric relief valve of installing on the pipeline between air-cooled oil product fractionation plant 2 and liquefied gas recovery and the condensation compression set 38; Entering into energy-saving gasification zero release boiler 10 through fireproof tempering device 11 burns; The waste residue of being discharged by waste residue relief outlet 9 is recycled to be proceeded in the energy-saving gasification zero release boiler 10 to burn, and various refuses are utilized once more.

Claims (4)

1. waste oil regeneration use device; Comprise that water cycle air extractor (1), air-cooled oil product fractionation plant (2), liquefied gas reclaim and condensation compression set (3); The top of air-cooled oil product fractionation plant (2) is reclaimed with liquefied gas through pipeline and is connected with condensing works (3); Inside is provided with four and receives oil tray (5); Water cycle air extractor (1) is connected with air-cooled oil product fractionation plant (2) through pipeline; It is characterized in that: the top of water cycle air extractor (1) links to each other through pipeline and raw material intensification jar (6), and the inside of raw material intensification jar (6) is provided with heating pipeline (6-1), and an end of the pipeline (6-1) that generates heat is connected with energy-saving gasification zero release boiler (10); On the pipeline of air-cooled oil product fractionation plant (2) and liquefied gas recovery and condensation compression set (3) atmospheric relief valve (8) is installed, atmospheric relief valve (8) is connected with energy-saving gasification zero release boiler (10) through gas transmission pipeline.
2. a kind of waste oil regeneration use device according to claim 1 is characterized in that: the side top of raw material intensification jar (6) is equipped with negative pressure relief valve (7), and inner and upper is equipped with receives oil tray (5).
3. a kind of waste oil regeneration use device according to claim 1 is characterized in that: water level limitation device (2-5) is equipped with in the bottom of air-cooled oil product fractionation plant (2), and is positioned at the top of the pipeline that connects water cycle air extractor (1).
4. a kind of waste oil regeneration use device according to claim 1 is characterized in that: fireproof tempering device (11) is installed in the gas transmission pipeline.
CN 201220289795 2012-06-20 2012-06-20 Waste oil recycling device Expired - Lifetime CN202626115U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220289795 CN202626115U (en) 2012-06-20 2012-06-20 Waste oil recycling device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220289795 CN202626115U (en) 2012-06-20 2012-06-20 Waste oil recycling device

Publications (1)

Publication Number Publication Date
CN202626115U true CN202626115U (en) 2012-12-26

Family

ID=47379335

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220289795 Expired - Lifetime CN202626115U (en) 2012-06-20 2012-06-20 Waste oil recycling device

Country Status (1)

Country Link
CN (1) CN202626115U (en)

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right

Effective date of registration: 20190124

Address after: 518040 East Block 3 378, 206 Tairan Science Park, Tairan 7 Road, Shatou Street, Futian District, Shenzhen City, Guangdong Province

Patentee after: Shenzhen Huayong Environmental Engineering Co.,Ltd.

Address before: 753400 Xiamiao Repair Plant at the Intersection of Nuanquan Village, Chonggang Town, Pingluo County, Shizuishan City, Ningxia Hui Autonomous Region

Patentee before: Qi Wanren

TR01 Transfer of patent right
CX01 Expiry of patent term

Granted publication date: 20121226

CX01 Expiry of patent term