Device for treating oil dirt in sewage with rotational flow method and removal method of oil dirt in sewage with rotational flow method

A technology for oil pollution and sewage, which is applied to the cyclone method to treat oil pollution in sewage and its removal field, can solve the problems of land occupation, system maintenance, and high use costs, and achieve the improvement of the oil pollution purification rate, the oil pollution purification rate is remarkable, and the scope of application expansive effect

Inactive Publication Date: 2016-07-13
XUZHOU INSTITUTE OF TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] Among them, since each set of water treatment equipment cannot independently achieve the target value of pretreatment, a system composed of multiple equipment in series and parallel is required to complete the com

Method used

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  • Device for treating oil dirt in sewage with rotational flow method and removal method of oil dirt in sewage with rotational flow method
  • Device for treating oil dirt in sewage with rotational flow method and removal method of oil dirt in sewage with rotational flow method
  • Device for treating oil dirt in sewage with rotational flow method and removal method of oil dirt in sewage with rotational flow method

Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

[0050] Example 1

[0051] In parts by weight, the oil-absorbing particles 3-4-1 of the present invention are manufactured according to the following steps:

[0052] Step 1: Add 250 parts of ultrapure water with a conductivity of 0.02μS / cm to the reactor, start the stirrer in the reactor, rotate at 90rpm, start the heat pump, and increase the temperature in the reactor to 52℃; add sequentially Rare earth phosphate 12 parts, acetaldehyde n-propyl mercaptan acetal 16 parts, 2-methoxyacetaldehyde dimethyl acetal 8 parts, stir until completely dissolved, adjust the pH to 3.7, adjust the stirrer speed to 113rpm, temperature At 63°C, esterification reaction for 3.5 hours;

[0053] Step 2: Take 1 part of 2-ethylhexanal cycloethylene acetal, 9 parts of dimethyl chloroacetal, powder particle size of 310 mesh; add 18 parts of formaldehyde diethylene glycol monobutyl ether and mix Evenly, spread in the tray with a thickness of 11mm, with a dose of 2.2kGy and an energy of 6.2MeV α-ray irradiati...

Example Embodiment

[0057] Example 2

[0058] In parts by weight, the oil-absorbing particles 3-4-1 of the present invention are manufactured according to the following steps:

[0059] Step 1: Add 750 parts of ultrapure water with a conductivity of 0.09μS / cm to the reactor, start the stirrer in the reactor, rotate at 160rpm, start the heat pump, and increase the temperature in the reactor to 73℃; add sequentially 55 parts of rare earth phosphate, 27 parts of acetaldehyde n-propyl mercaptan acetal, 35 parts of 2-methoxyacetaldehyde dimethyl acetal, stir until completely dissolved, adjust the pH to 8.8, adjust the stirrer speed to 178rpm, temperature At 98°C, the esterification reaction is 17 hours;

[0060] Step 2: Take 13 parts of 2-ethylhexanal cycloethylene acetal, 22 parts of dimethyl chloroacetal, powder particle size of 800 mesh; add 45 parts of formaldehyde diethylene glycol monobutyl ether and mix Evenly spread in the tray with a thickness of 29mm, irradiated by alpha rays with a dose of 5.4kGy...

Example Embodiment

[0064] Example 3

[0065] In parts by weight, the oil-absorbing particles 3-4-1 of the present invention are manufactured according to the following steps:

[0066] Step 1: Add 259 parts of ultrapure water with a conductivity of 0.029μS / cm to the reactor, start the stirrer in the reactor, rotate at 99 rpm, start the heat pump, and increase the temperature in the reactor to 59°C; add sequentially 17 parts of rare earth phosphate, 18 parts of acetaldehyde n-propyl mercaptan acetal, 18 parts of 2-methoxyacetaldehyde dimethylacetal, stir until completely dissolved, adjust the pH to 4.8, adjust the stirrer speed to 118rpm, temperature At 68°C, the esterification reaction is 3.9 hours;

[0067] Step 2: Take 11 parts of 2-ethylhexanal cycloethylene acetal, 13 parts of dimethyl chloroacetal, powder particle size of 314 mesh; add 21 parts of formaldehyde diethylene glycol monobutyl ether and mix Evenly spread in the tray with a thickness of 19mm, with a dose of 2.9kGy and an energy of 6.78M...

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Abstract

The invention discloses a device for treating oil dirt in sewage with a rotational flow method and a removal method of the oil dirt in sewage with rotational flow method. The device is composed of a sewage tank, a water conveying device, an oil removing and precipitation tank, a rotational flow oil collection device, a clean water discharging pipe, an oil dirt discharging pipe, a sludge discharging pipe, a sludge tank, a bracket and a control system, wherein sewage enters the oil removing and precipitation tank from the bottom through the water conveying device; treated clean water is discharged out of a tank body through the clean water discharging pipe; the oil dirt is discharged out of the tank body through the oil dirt discharging pipe; and impurities are discharged into the sludge tank through the sludge discharging pipe. The device for treating oil dirt in sewage with the rotational flow method and the removal method of the oil dirt, disclosed by the invention, have the advantages of novel and reasonable structure, high oil dirt removing rate and wide applicable range.

Description

technical field [0001] The invention belongs to the field of sewage treatment devices, and in particular relates to a device for treating oil in sewage by a cyclone method and a removal method thereof. Background technique [0002] A large amount of oily sewage is produced in the process of oil and gas fields and petrochemical production. The oily sewage contains crude oil, suspended solids and other complex mineral impurities, which must be treated. Direct discharge will pollute the environment, and direct reinjection will cause formation pollution. [0003] In the existing technology, in order to remove crude oil and suspended solids in oily sewage, oily sewage in oil and gas fields is usually completed by vertical gravity deoiling tanks and vertical coagulation settling tanks, while oily sewage in petrochemical The oil separation sedimentation tank is completed; the follow-up generally adopts inclined plate oil separation or air flotation, coarse granulation and multi-med...

Claims

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Application Information

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IPC IPC(8): B01D21/02B01D17/038
CPCB01D17/0217B01D21/02
Inventor 张建昆
Owner XUZHOU INSTITUTE OF TECHNOLOGY
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