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Treatment method of waste drilling fluid

The technology of a waste drilling fluid and a treatment method, which is applied to the treatment field of waste drilling fluid, can solve the problems of high processing cost, insufficient recovery, and pollution of crude oil contained in the environment, and achieves low energy consumption, simple processing links and high efficiency. high effect

Active Publication Date: 2014-04-30
陕西环保恒润工程有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The purpose of the present invention is to provide a treatment method for waste drilling fluid, which can solve the problems of high treatment cost, environmental pollution and insufficient recovery of crude oil contained in waste drilling fluid due to high water content of waste drilling fluid, and realize waste drilling Harmless and resourceful liquid

Method used

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  • Treatment method of waste drilling fluid

Examples

Experimental program
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Effect test

Embodiment 1

[0017] Waste drilling fluid flow rate is 400m 3 / h, in the rectangular advection sloping plate grease trap 2 with a length×width×height of 20000mm×6000mm×2200mm, the sloping plate module is installed on the bracket in the steel tank, and the specifications of the sloping plate used are as follows: plate length 1550mm, slab width 650mm, slab thickness 1.6mm, each slab has 11 waves, wavelength 59mm, wave height 30mm, sloping plate spacing 30mm, inclination angle 45 degrees, advection sloping plate grease trap 2 residence time 30min , can remove oil particles and most solid particles above 60μm. The material and structure of the primary degreasing filter 3 and the secondary degreasing filter 4 are exactly the same, the two operate in series, the flow coefficient of clean water is a=0.7, the inside of the degreasing filter is filled with fruit shell activated carbon filter material, and the thickness of the filter layer is 1.40m , packing density 600kg / m 3 , particle size 40 mes...

Embodiment 2

[0019] Waste drilling fluid flow rate 340m 3 / h, in the rectangular advection inclined plate grease trap 2 with a length × width × height of 18000mm × 5500mm × 2200mm, inclined plate modules are installed on the brackets in the steel pool, and the specifications of the inclined plates used are as follows: plate length 1550mm, slab width 650mm, slab thickness 1.6mm, each slab has 11 waves, wavelength 59mm, wave height 30mm, sloping plate spacing 30mm, inclination angle 45 degrees, advection sloping plate grease trap residence time 30min, It can remove oil particles and most solid particles above 60μm. The material and structure of the primary degreasing filter 3 and the secondary degreasing filter 4 are exactly the same, the two operate in series, the flow coefficient of clean water is a=0.7, the inside of the degreasing filter is filled with fruit shell activated carbon filter material, and the thickness of the filter layer is 1.40m , packing density 500kg / m 3 , particle siz...

Embodiment 3

[0021] Waste drilling fluid flow rate 210m 3 / h, in the rectangular advection sloping plate grease trap 2 with a length × width × height of 14000mm × 4500mm × 2200mm, the slant plate modules are installed on the brackets in the steel pool, and the specifications of the slant plates used are as follows: plate length 1550mm, slab width 650mm, slab thickness 1.60mm, each slab has 11 waves, wavelength 59mm, wave height 30mm, sloping plate spacing 30mm, inclination angle 45 degrees, advection sloping plate grease trap residence time 30min, It can remove oil particles and most solid particles above 60μm. The material and structure of the primary degreasing filter 3 and the secondary degreasing filter 4 are exactly the same, the two operate in series, the flow coefficient of clean water is a=0.7, the inside of the degreasing filter is filled with fruit shell activated carbon filter material, and the thickness of the filter layer is 1.30m , packing density 600kg / m3 , particle size 30...

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Abstract

The invention discloses a treatment method of waste drilling fluid. The treatment method includes: delivering waste drilling fluid into a mixing tank, injecting water-soluble demulsifier into the mixing tank, mixing, and delivering mixture to a horizontal-flow inclined-plate oil separator; transferring upper floating oil to a gravitational coil collecting tank; transferring bottom sludge to a sludge conditioning tank, adding sludge conditioner into the sludge conditioning tank, mixing the sludge conditioner with sludge, sending mixture into a sludge delivery pipe, injecting flocculant at the tail end of the sludge delivery pipe, sending the sludge into a horizontal-screw discharge and sedimentation centrifuge for dewatering, allowing separated water obtained by dewatering to flow back into the horizontal-flow inclined-plate oil separator; allowing waste water flowing out of the horizontal-flow inclined-plate oil separator to sequentially flow into a primary deoiling filter and a secondary deoiling filter for filtration and oil removal; and transferring floating oil from the top of each of the horizontal-flow inclined-plate oil separator, the first deoiling filter and the second deoiling filter into a gravitational oil collecting tank for oil and water separation. Waste is comprehensive recycled harmlessly.

Description

technical field [0001] The invention belongs to the technical field of "three wastes" treatment in the oil exploitation industry, and in particular relates to a treatment method for waste drilling fluid. Background technique [0002] Drilling fluid is an engineering fluid used in the drilling and mining process of the petroleum industry. It can complete many key tasks such as suspension, pressure control, rock formation stability, buoyancy, lubrication and cooling during drilling. The used waste drilling fluid and drilling cuttings contaminated by drilling fluid are collected in the well site collection pool, collectively referred to as waste drilling fluid. The collected waste drilling fluid is a mixture of oily sewage and sludge, which has the characteristics of large volume, low solid content, high water content, large oil content, fine particles, high viscosity, and difficult dehydration. [0003] At present, domestic oilfields generally adopt direct solidification trea...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C02F9/04C02F11/12C02F103/10
Inventor 张文艺张采芹刘春节郑泽鑫李仁霞
Owner 陕西环保恒润工程有限公司