CN205907130U - Device of oil field sewage biochemical treatment accuse temperature - Google Patents

Device of oil field sewage biochemical treatment accuse temperature Download PDF

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Publication number
CN205907130U
CN205907130U CN201620695045.XU CN201620695045U CN205907130U CN 205907130 U CN205907130 U CN 205907130U CN 201620695045 U CN201620695045 U CN 201620695045U CN 205907130 U CN205907130 U CN 205907130U
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China
Prior art keywords
temperature
intensification
cooling
surge tank
detecting device
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CN201620695045.XU
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Chinese (zh)
Inventor
潘永强
袁长忠
王静
段传慧
胡静
孙刚正
宋欣
冯云
谭晓明
吴晓玲
张守献
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China Petroleum and Chemical Corp
Sinopec Research Institute of Petroleum Engineering Shengli Co
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China Petroleum and Chemical Corp
Sinopec Research Institute of Petroleum Engineering Shengli Co
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Abstract

The utility model belongs to the technical field of sewage treatment, concretely relates to device of oil field sewage biochemical treatment accuse temperature, including looping through pipeline connection's settling basin, biochemical pond and ultrafiltration device, still include intensification system, cooling system and temperature and flow control system, the intensification system comes water line, temperature rising coiled pipe, intensification recovery pipeline and intensification stop valve to form by intensification buffer tank, intensification flowmeter, intensification, cooling system comes water line, cooling flowmeter, cooling coil, cooling recovery pipeline and cooling stop valve to form by cooling buffer tank, cooling, the temperature comprises temperature and flow controller, biochemical pond temperature -detecting device, cooling buffer tank temperature -detecting device, intensification buffer tank temperature -detecting device, cooling solenoid valve and intensification solenoid valve with flow control system. The utility model has the characteristics of simple structure, safe and reliable, degree of automation height and energy -concerving and environment -protective advantage. Therefore, the utility model discloses can be applied to widely among the sewage biochemical treatment technical field.

Description

A kind of device of oilfield sewage biochemical treatment temperature control
Technical field
This utility model belongs to technical field of sewage and in particular to a kind of dress of oilfield sewage biochemical treatment temperature control Put.
Background technology
Current oilfield sewage carries out process frequently with the technique that natural subsidence, biochemical treatment and ultrafiltration combine and realizes sewage Outer row or re-injection.Biochemical treatment is the polluter being processed by the metabolism of microorganism in waste water, typically may be used To be divided into aerobic and two kinds of anaerobic treatment.Because microorganism needs growth metabolism in certain reservoir media, temperature is to micro- life The impact of thing is the most notable, the temperature general control in sewage disposal mesophytization pond in the range of 20~35 DEG C, oilfield sewage Carry out coolant-temperature gage typically at 50~70 DEG C, sewage disposal device when running in winter due to pipeline cooling substantially, the temperature of biochemistry pool Far below the temperature needed for biochemistry pool, the mode heating frequently with electrical bar at present maintains the temperature of biochemistry pool, but adopts electric heating The mode of rod heating has power consumption greatly, and maintenance cost is high, and heating is uneven, haves the shortcomings that potential safety hazard simultaneously;And summer Because outdoor temperature is higher when equipment runs, highest is more than 40 DEG C it is impossible to ensure the normal operation of biochemistry pool.
Content of the invention
This utility model is directed to the deficiencies in the prior art and provides a kind of device of oilfield sewage biochemical treatment temperature control, this dress Put to have and rise two kinds of functions of gently lowering the temperature it is ensured that biochemistry pool can normal operation under complicated weather condition;The heating of this device is all Even, there is not localized hyperthermia;There is energy-conserving and environment-protective, safe and reliable, simple to operate and high degree of automation simultaneously.
The utility model discloses a kind of device of oilfield sewage biochemical treatment temperature control, including passing sequentially through pipeline connection Sedimentation tank, biochemistry pool and ultrafiltration apparatus it is characterised in that described device also include temperature elevation system, cooling system and temperature with Flow control system;Described temperature elevation system is by the surge tank that heats up, intensification effusion meter, heat up water pipeline, intensification coil pipe, intensification Recovery line and intensification stop valve composition, described intensification carrys out water pipeline and is sequentially connected intensification surge tank, intensification effusion meter and liter The entrance of Winchester disk pipe, described rising temperature reclamation pipeline is sequentially connected the outlet of intensification coil pipe, intensification stop valve and intensification surge tank; Described cooling system comes water pipeline, cooling effusion meter, temperature-reducing coil, lowered temperature reclamation pipeline and fall by surge tank of lowering the temperature, cooling Warm stop valve composition;Described cooling carrys out water pipeline and is sequentially connected cooling surge tank, cooling effusion meter, the entrance of temperature-reducing coil; Described lowered temperature reclamation pipeline is sequentially connected outlet, cooling stop valve and the cooling surge tank of temperature-reducing coil;Described temperature with Flow control system is by temperature and flow controller, biochemistry pool temperature-detecting device, cooling surge tank temperature-detecting device, intensification Surge tank temperature-detecting device, cooling electromagnetic valve and intensification electromagnetic valve composition, described temperature passes through signal with flow controller Line connects biochemistry pool temperature-detecting device, cooling surge tank temperature-detecting device, intensification surge tank temperature-detecting device, cooling electricity Magnet valve, intensification electromagnetic valve, intensification effusion meter and cooling effusion meter, described biochemistry pool temperature-detecting device detects the temperature of biochemistry pool Degree, the temperature of cooling surge tank temperature-detecting device detection cooling surge tank, the detection of intensification surge tank temperature-detecting device heats up The temperature of surge tank, intensification electromagnetic valve is arranged on cooling between cooling surge tank and cooling effusion meter and comes on water pipeline, cooling electricity Magnet valve is arranged on and heats up on water pipeline between intensification surge tank and intensification effusion meter.
Wherein, the volume of described intensification surge tank is 0.8-1.0m3, the volume of cooling surge tank is 0.5-0.8m3.
The range of flow of described intensification effusion meter and cooling effusion meter detection is 0-20m3/h.
Described intensification coil pipe is arranged on the inside of biochemistry pool, and it is highly made a living for the 4/5-5/6 of biochemistry pool height, width Change the 2/3-3/4 of pond width.
Described temperature-reducing coil is arranged on the inside of Sedimentation tank, and it is heavy highly for the 4/5-5/6 of Sedimentation tank height, width The 2/3-3/4 of fall pond width.
The material of the gentle temperature-reducing coil of described liter is pyrite.
The temperature range of described cooling surge tank temperature-detecting device and the detection of intensification surge tank temperature-detecting device is equal For 0-150 DEG C.
This utility model compared with prior art has the advantage that and beneficial effect:
(1) structure is simple, operate simple, multiple functional, high degree of automation;
(2) intensification coil pipe of the present utility model has homogeneous heating, there is not localized hyperthermia;
(3) there is no heating source, there is not potential safety hazard, safe and reliable;
(4) this utility model realizes the constant temperature of biochemistry pool using the high temperature of water and the low temperature of water outlet, rises gentle cooling Sewage afterwards returns surge tank, has the advantages that energy-conserving and environment-protective.
Brief description
Accompanying drawing 1 is the structure flow chart of the device of oilfield sewage biochemical treatment temperature control.
Specific embodiment
Refering to accompanying drawing 1, a kind of device of oilfield sewage biochemical treatment temperature control, including the sedimentation passing sequentially through pipeline connection Pond, biochemistry pool and ultrafiltration apparatus, this device also includes temperature elevation system 1, cooling system 2 and temperature and flow control system 3;Described Temperature elevation system 1 by intensification surge tank 11, intensification effusion meter 12, heat up come water pipeline 13, intensification coil pipe 14, rising temperature reclamation pipeline 15 and intensification stop valve 16 form, described intensification carrys out water pipeline 13 and is sequentially connected intensification surge tank 11, intensification effusion meter 12 and The entrance of intensification coil pipe 14, described rising temperature reclamation pipeline 15 is sequentially connected the outlet of intensification coil pipe 14, intensification stop valve 16 and Intensification surge tank 11;Described cooling system 2 comes water pipeline 22, cooling effusion meter 23, cooling plate by cooling surge tank 21, cooling Pipe 24, lowered temperature reclamation pipeline 25 and cooling stop valve 26 form;Described cooling carrys out water pipeline 22 and is sequentially connected cooling surge tank 21st, cooling effusion meter 23, the entrance of temperature-reducing coil 24;Described lowered temperature reclamation pipeline 25 is sequentially connected going out of temperature-reducing coil 24 Mouth, cooling stop valve 26 and cooling surge tank 21;Described temperature and flow control system 3 by temperature and flow controller 31, Biochemistry pool temperature-detecting device 32, cooling surge tank temperature-detecting device 33, intensification surge tank temperature-detecting device 34, cooling electricity Magnet valve 35 and intensification electromagnetic valve 36 form, and described temperature is connected biochemistry pool temperature detection with flow controller 31 by holding wire Device 32, cooling surge tank temperature-detecting device 33, intensification surge tank temperature-detecting device 34, cooling electromagnetic valve 35, intensification electricity Magnet valve 36, intensification effusion meter 12 and cooling effusion meter 23, described biochemistry pool temperature-detecting device 32 detects the temperature of biochemistry pool, The temperature of cooling surge tank temperature-detecting device 33 detection cooling surge tank 21, intensification surge tank temperature-detecting device 34 detection rises The temperature of warm surge tank 11, intensification electromagnetic valve 35 is arranged on cooling between cooling surge tank 21 and cooling effusion meter 23 and carrys out water pipeline On 22, cooling electromagnetic valve 36 is arranged on and heats up on water pipeline 13 between intensification surge tank 11 and intensification effusion meter 12.
Wherein, the volume of intensification surge tank 11 is 0.8-1.0m3, the volume of cooling surge tank 21 is 0.5-0.8m3;Heat up The range of flow of effusion meter 12 and cooling effusion meter 23 detection is 0-20m3/h;Intensification coil pipe 14 is arranged on the interior of biochemistry pool Portion, it is the 2/3-3/4 of biochemistry pool width highly for the 4/5-5/6 of biochemistry pool height, width;Temperature-reducing coil 24 is arranged on sedimentation The inside in pond, it is the 2/3-3/4 of Sedimentation tank width highly for the 4/5-5/6 of Sedimentation tank height, width;Rise gentle temperature-reducing coil Material be pyrite;Cooling surge tank temperature-detecting device 33 and the temperature model of intensification surge tank temperature-detecting device 34 detection Enclose equal 0-150 DEG C.

Claims (7)

1. a kind of device of oilfield sewage biochemical treatment temperature control, including passing sequentially through the Sedimentation tank of pipeline connection, biochemistry pool and super Filter device is it is characterised in that described device also includes temperature elevation system, cooling system and temperature and flow control system;Described Temperature elevation system by the surge tank that heats up, intensification effusion meter, heat up come water pipeline, intensification coil pipe, rising temperature reclamation pipeline and heat up cut Only valve group becomes, and described intensification carrys out the entrance that water pipeline is sequentially connected intensification surge tank, intensification effusion meter and intensification coil pipe, described Rising temperature reclamation pipeline be sequentially connected the outlet of intensification coil pipe, intensification stop valve and intensification surge tank;Described cooling system by Cooling surge tank, cooling come water pipeline, cooling effusion meter, temperature-reducing coil, lowered temperature reclamation pipeline and cooling stop valve composition;Described Cooling come water pipeline be sequentially connected cooling surge tank, cooling effusion meter, the entrance of temperature-reducing coil;Described lowered temperature reclamation pipeline It is sequentially connected outlet, cooling stop valve and the cooling surge tank of temperature-reducing coil;Described temperature and flow control system are by temperature With flow controller, biochemistry pool temperature-detecting device, cooling surge tank temperature-detecting device, intensification surge tank temperature detection dress Put, lower the temperature electromagnetic valve and intensification electromagnetic valve composition, described temperature is connected biochemistry pool temperature with flow controller by holding wire Detection means, cooling surge tank temperature-detecting device, intensification surge tank temperature-detecting device, cooling electromagnetic valve, intensification electromagnetic valve, Intensification effusion meter and cooling effusion meter, described biochemistry pool temperature-detecting device detects the temperature of biochemistry pool, surge tank temperature of lowering the temperature The temperature of degree detection means detection cooling surge tank, intensification surge tank temperature-detecting device detects the temperature of intensification surge tank, rises Warm electromagnetic valve is arranged on cooling between cooling surge tank and cooling effusion meter and comes on water pipeline, and it is slow that cooling electromagnetic valve is arranged on intensification Rush and heat up on water pipeline between tank and intensification effusion meter.
2. the device of oilfield sewage biochemical treatment temperature control according to claim 1 is it is characterised in that described intensification buffers The volume of tank is 0.8-1.0m3, the volume of cooling surge tank is 0.5-0.8m3.
3. the device of oilfield sewage biochemical treatment temperature control according to claim 1 and 2 is it is characterised in that described intensification The range of flow of effusion meter and cooling effusion meter detection is 0-20m3/h.
4. the device of oilfield sewage biochemical treatment temperature control according to claim 1 and 2 is it is characterised in that described intensification Coil pipe is arranged on the inside of biochemistry pool, and it is the 2/3-3/4 of biochemistry pool width highly for the 4/5-5/6 of biochemistry pool height, width.
5. the device of oilfield sewage biochemical treatment temperature control according to claim 4 is it is characterised in that described temperature-reducing coil It is arranged on the inside of Sedimentation tank, it is the 2/3-3/4 of Sedimentation tank width highly for the 4/5-5/6 of Sedimentation tank height, width.
6. the device of oilfield sewage biochemical treatment temperature control according to claim 5 is it is characterised in that described liter gently drops The material of Winchester disk pipe is pyrite.
7. the device of the oilfield sewage biochemical treatment temperature control according to claim 1 or 6 is it is characterised in that described cooling The temperature range of surge tank temperature-detecting device and the detection of intensification surge tank temperature-detecting device is 0-150 DEG C.
CN201620695045.XU 2016-07-01 2016-07-01 Device of oil field sewage biochemical treatment accuse temperature Active CN205907130U (en)

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Application Number Priority Date Filing Date Title
CN201620695045.XU CN205907130U (en) 2016-07-01 2016-07-01 Device of oil field sewage biochemical treatment accuse temperature

Publications (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107555706A (en) * 2016-07-01 2018-01-09 中国石油化工股份有限公司 A kind of device and method of oilfield sewage biochemical treatment temperature control

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107555706A (en) * 2016-07-01 2018-01-09 中国石油化工股份有限公司 A kind of device and method of oilfield sewage biochemical treatment temperature control

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