CN207980470U - A kind of fractionating column and the online demineralizer of water cooler - Google Patents

A kind of fractionating column and the online demineralizer of water cooler Download PDF

Info

Publication number
CN207980470U
CN207980470U CN201820203821.9U CN201820203821U CN207980470U CN 207980470 U CN207980470 U CN 207980470U CN 201820203821 U CN201820203821 U CN 201820203821U CN 207980470 U CN207980470 U CN 207980470U
Authority
CN
China
Prior art keywords
water
regulating valve
water cooler
connection
fractionating column
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201820203821.9U
Other languages
Chinese (zh)
Inventor
李强
杨文清
杨龙
刘晓海
门彦杰
魏艳艳
史桂清
许连杰
耿斌强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Zhenghe Group Co Ltd
Original Assignee
Zhenghe Group Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhenghe Group Co Ltd filed Critical Zhenghe Group Co Ltd
Priority to CN201820203821.9U priority Critical patent/CN207980470U/en
Application granted granted Critical
Publication of CN207980470U publication Critical patent/CN207980470U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The utility model discloses a kind of fractionating columns and the online demineralizer of water cooler, including fractionating column, water cooler, rotation oil dehydrator, gun barrel, sewage disposal system, circulating pump, flow line, injection manifold line, connecting pipeline, regulating valve and autocontrol valve;The end of the injection manifold line forms three branches, respectively installs the first by-pass line of water filling of the first regulating valve, installs the second by-pass line of water filling of the second regulating valve and installs the water filling third by-pass line of third regulating valve.The utility model compared with prior art, stablize, be safe and efficient by easy for installation, easy to operate, operating;Fractionation tower top can be effectively relieved and follow system salt crust speed, reduce the extent of corrosion that pipeline is followed on fractionating column top tray, tower wall and top;It effectively prevent cooler salt crust;It is carried out at the same time water-oil separation and the sewage to separating carries out purified treatment;Reduce the loss of shut-down water-flushed zone.

Description

A kind of fractionating column and the online demineralizer of water cooler
Technical field
The utility model is related to petroleum chemical industries, and in particular to a kind of fractionating column and the online demineralizer of water cooler.
Background technology
In refining oil fractional distillation process, because fractionation tower temperature reduces, there is water phase appearance, lead to delayed coking unit fractionating column System salt crust is followed on top and corrosion is extremely serious.The phenomenon that top is followed after system salt crust, fouling makes system pressure difference increase, petrol and diesel oil production Product separation is unintelligible, and fractionating column rushes tower, and top follows pump depletion, influences the safety in production of device;Also amine salt NH4Cl in part generally exists It is precipitated at cooler, affects the working effect of cooler, sometimes because repair can only shutdown process.
Utility model content
The purpose of this utility model is in view of the above technical problems, to provide a kind of fractionating column and the online desalination dress of water cooler It sets, fractionation tower top can be effectively relieved and follow system salt crust speed, prevent water cooler salt crust, it is ensured that safety in production and cooling effect Fruit.
The purpose of this utility model is achieved through the following technical solutions:
A kind of fractionating column and the online demineralizer of water cooler, including fractionating column, water cooler, rotation oil dehydrator, water-oil separating Tank, sewage disposal system, circulating pump, flow line, injection manifold line, connecting pipeline, regulating valve and autocontrol valve;Described point Evaporate the oil outlet of top of tower setting connection flow line;The water cooler includes the first water cooler, the second water cooler and third water Cooler;The mouth of a river is provided in the water-oil separating pot bottom;The circulating pump includes first circulation pump and second circulation pump;The tune It includes the first regulating valve, the second regulating valve and third regulating valve to save valve, and its control terminal is connect with circuit control device;It is described The end of injection manifold line forms three branches, respectively installs the first by-pass line of water filling of the first regulating valve, installation second is adjusted It saves the second by-pass line of water filling of valve and the water filling third by-pass line of third regulating valve is installed;The connecting pipeline includes the first connection Pipeline, the second connecting pipeline, third connecting pipeline, the 4th connecting pipeline and the 5th connecting pipeline;First connecting pipeline Autocontrol valve is installed at the top of one end connection fractionating column top side, other end connection rotation oil dehydrator, on pipeline;Described second One end of connecting pipeline is connected in the first connecting pipeline, the other end pumps connection water-oil separating tank top one by second circulation Side;One end of the third connecting pipeline pumps connection fractionating column top side, other end connection rotation oil dehydration by second circulation Device top side is equipped with the first injection point of connection the first by-pass line of water filling, connection the second by-pass line of water filling on pipeline successively Second injection point and the third injection point for connecting water filling third by-pass line, and the first water cooling is installed after the first injection point Third water cooler is installed after second water cooler, third injection point are installed after device, the second injection point;The one of 4th connecting pipeline End connection rotation oil dehydrator bottom, the other end connect gun barrel top side;One end of 5th connecting pipeline connects Water-oil separating pot bottom water outlet, the other end connect sewage disposal system.
Said program can advanced optimize for:
The circuit control device includes power module, MCU Microprocessor Control Unit, analog-to-digital conversion module, time detection mould Block, regulating valve drive module and intermodule connection line.
The sewage disposal system includes biological treatment mechanism.
The biological treatment mechanism includes biofilter.
The utility model compared with prior art, stablize, be safe and efficient by easy for installation, easy to operate, operating;It can be effective Alleviate fractionation tower top and follow system salt crust speed, reduces the extent of corrosion that pipeline is followed on fractionating column top tray, tower wall and top;It is effectively anti- Only cooler salt crust;It is carried out at the same time water-oil separation and the sewage to separating carries out purified treatment;Reduce shut-down water-flushed zone Loss.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model;
Fig. 2 is the utility model circuit control device composition schematic diagram;
In figure:1- fractionating columns, 1.1- oil outlets, 2- injection manifold lines, the first by-pass line of 2.1- water fillings, 2.2- water fillings second By-pass line, 2.3- water filling third by-pass lines, the first water coolers of 3-, the second water coolers of 4-, 5- third water coolers, 6- first are adjusted Valve, the second regulating valves of 7-, 8- third regulating valves, 9- rotation oil dehydrators, 10- gun barrels, 10.1- water outlets, 11- are controlled automatically Valve processed, 12- sewage disposal systems, 13- first circulations pump, 14- second circulations pump, 15- flow lines, the first connecting pipelines of 16-, The second connecting pipelines of 17-, 18- third connecting pipelines, the first injection points of 18.1-, the second injection points of 18.2-, 18.3- third water fillings Point, the 4th connecting pipelines of 19-, the 5th connecting pipelines of 20-, 21- MCU Microprocessor Control Units, 22- time detection modules, 23- tune Save valve drive module, 24- analog-to-digital conversion modules, 25- power modules.
Specific implementation mode
The utility model is described in detail below in conjunction with the accompanying drawings.
Referring to Fig. 1, Fig. 2.A kind of fractionating column and the online demineralizer of water cooler, including fractionating column 1, water cooler, rotation oil are de- Hydrophone 9, gun barrel 10, sewage disposal system 12, circulating pump 13, flow line 15, injection manifold line 2, connecting pipeline, tune Save valve and autocontrol valve 11.The oil outlet 1.1 of 1 top setting connection flow line 15 of fractionating column.Water cooler includes the first water Cooler 3, the second water cooler 4 and third water cooler 5.Water outlet 10.1 is arranged in 10 bottom of gun barrel.Circulating pump includes first Circulating pump 13 and second circulation pump 14.Regulating valve includes the first regulating valve 6, the second regulating valve 7 and third regulating valve 8, and it is controlled End processed is connect with circuit control device.Circuit control device includes power module 25, MCU Microprocessor Control Unit 21, modulus turn Change the mold block 24, time detection module 22, regulating valve drive module 23 and intermodule connection line.The end shape of injection manifold line 2 At three branches, the first by-pass line of water filling 2.1 of the first regulating valve 6 is respectively installed, the water filling second of the second regulating valve 7 is installed The water filling third by-pass line 2.3 of by-pass line 2.2 and installation third regulating valve 8.Connecting pipeline includes the first connecting pipeline 16, second Connecting pipeline 17, third connecting pipeline 18, the 4th connecting pipeline 19 and the 5th connecting pipeline 20.One end of first connecting pipeline 16 Connect 1 top side of fractionating column, 9 top of oil dehydrator is revolved in other end connection, installs autocontrol valve 11 on pipeline.Second connection One end of pipeline 17 is connected in the first connecting pipeline 16, the other end passes through 14 connection gun barrel of second circulation pump, 10 top Side.One end of third connecting pipeline 18 is de- by 14 1 top side of connection fractionating column of second circulation pump, other end connection rotation oil 9 top side of hydrophone is equipped with the first injection point 18.1 of the first by-pass line of connection water filling 2.1, connection water filling the on pipeline successively The third injection point 18.3 of second injection point 18.2 of two by-pass lines 2.2 and connection water filling third by-pass line 2.3, and respectively at the Second water cooler 4, third injection point 18.3 are installed after first water cooler 3, the second injection point 18.2 are installed after one injection point 18.1 Installation third water cooler 5 afterwards.One end 9 bottom of connection rotation oil dehydrator of 4th connecting pipeline 19, the other end connect water-oil separating 10 top side of tank.One end 10 bottom water outlet 10.1 of connection gun barrel of 5th connecting pipeline 20, other end connection are dirty Water treatment system 12.To improve wastewater treatment efficiency, sewage disposal system 12 includes biofilter.
The basic functional principle and flow of the utility model are as follows:
When on-line operation, injection manifold line 2 is by each water filling by-pass line to 18 water filling of third connecting pipeline.Circuit controller Power module 25 provides power supply to circuit control device in part, and analog-to-digital conversion module 24 is according to water cooler salt crust situation by transformation Signal is handled by time detection module 22 and MCU Microprocessor Control Unit 21, then by regulating valve drive module 23 to not It is turned on and off with the regulating valve on water filling by-pass line, realization is supplied water respectively to each water cooler or central water supply.Third connects Enter rotation oil dehydrator 9 after the water cooled device cooling of grease in take over line 18, the oil phase after rotation oil dehydrator 9 detaches is by the One connecting pipeline 16 simultaneously carries out auto-control by autocontrol valve 11, is back to 1 top of fractionating column;Water contains in the oil phase isolated Amount is less than 100ppm.Saline sewage after being detached in revolving oil dehydrator 9 enters by hypocentrum export in gun barrel;Through A small amount of oil phase that gun barrel 10 is isolated is back to 1 top of fractionating column by the second connecting pipeline 17;Saliferous after separation Sewage enters sewage disposal system 12.The oil phase fractionated out in fractionating column 1 is exited by oil outlet 1.1 in next step Reason.

Claims (4)

1. a kind of fractionating column and the online demineralizer of water cooler, including fractionating column and water cooler, it is characterised in that:Further include rotation oil Dehydrator, gun barrel, sewage disposal system, circulating pump, flow line, injection manifold line, connecting pipeline, regulating valve and from Dynamic control valve;The oil outlet of setting connection flow line at the top of the fractionating column;The water cooler includes the first water cooler, second Water cooler and third water cooler;The mouth of a river is provided in the water-oil separating pot bottom;The circulating pump includes first circulation pump and the Two circulating pumps;The regulating valve include the first regulating valve, the second regulating valve and third regulating valve, and its control terminal with circuit control Device connection processed;The end of the injection manifold line forms three branches, respectively installs the water filling first of the first regulating valve Pipeline, the second by-pass line of water filling for installing the second regulating valve and the water filling third by-pass line for installing third regulating valve;The connection Pipeline includes the first connecting pipeline, the second connecting pipeline, third connecting pipeline, the 4th connecting pipeline and the 5th connecting pipeline;Institute The one end for stating the first connecting pipeline connects fractionating column top side, other end connection is revolved at the top of oil dehydrator, is installed certainly on pipeline Dynamic control valve;One end of second connecting pipeline is connected in the first connecting pipeline, the other end is pumped by second circulation and connected Gun barrel top side;One end of the third connecting pipeline pumps connection fractionating column top side, another by second circulation Oil dehydrator top side is revolved in one end connection, is equipped with the first injection point, the connection of connection the first by-pass line of water filling on pipeline successively Second injection point of the second by-pass line of water filling and the third injection point for connecting water filling third by-pass line, and respectively at the first injection point After install the second water cooler, third injection point are installed after the first water cooler, the second injection point after third water cooler is installed;Described One end connection rotation oil dehydrator bottom of four connecting pipelines, the other end connect gun barrel top side;5th connection One end connection water-oil separating pot bottom water outlet, the other end of pipeline connect sewage disposal system.
2. a kind of fractionating column according to claim 1 and the online demineralizer of water cooler, it is characterised in that:The circuit control Device processed includes power module, MCU Microprocessor Control Unit, analog-to-digital conversion module, time detection module, regulating valve drive module And intermodule connection line.
3. a kind of fractionating column according to claim 1 and the online demineralizer of water cooler, it is characterised in that:At the sewage Reason system includes biological treatment mechanism.
4. a kind of fractionating column according to claim 3 and the online demineralizer of water cooler, it is characterised in that:At the biology It includes biofilter to manage mechanism.
CN201820203821.9U 2018-02-06 2018-02-06 A kind of fractionating column and the online demineralizer of water cooler Active CN207980470U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201820203821.9U CN207980470U (en) 2018-02-06 2018-02-06 A kind of fractionating column and the online demineralizer of water cooler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201820203821.9U CN207980470U (en) 2018-02-06 2018-02-06 A kind of fractionating column and the online demineralizer of water cooler

Publications (1)

Publication Number Publication Date
CN207980470U true CN207980470U (en) 2018-10-19

Family

ID=63823899

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201820203821.9U Active CN207980470U (en) 2018-02-06 2018-02-06 A kind of fractionating column and the online demineralizer of water cooler

Country Status (1)

Country Link
CN (1) CN207980470U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109882736A (en) * 2019-03-19 2019-06-14 浙江理工大学 Adaptive intelligent flood pattern based on PID control
CN110068242A (en) * 2019-03-19 2019-07-30 浙江理工大学 Adaptive intelligent flood pattern and water-filling method based on PID control

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109882736A (en) * 2019-03-19 2019-06-14 浙江理工大学 Adaptive intelligent flood pattern based on PID control
CN110068242A (en) * 2019-03-19 2019-07-30 浙江理工大学 Adaptive intelligent flood pattern and water-filling method based on PID control
WO2020187338A1 (en) * 2019-03-19 2020-09-24 浙江理工大学 Pid control-based adaptive smart water injection system and water injection method
CN109882736B (en) * 2019-03-19 2020-11-20 浙江理工大学 Self-adaptive intelligent water injection system based on PID control

Similar Documents

Publication Publication Date Title
CN207980470U (en) A kind of fractionating column and the online demineralizer of water cooler
CN100453137C (en) Alcohol quinque-towel differential pressure distilling arrangement and technique thereof
CN101513232A (en) A novel ball water-boiling machine
CN102765842A (en) Pressure-reduction, alkali-addition and ammonia-distillation system
CN102519300A (en) Method for chemically and circularly cleaning scale inside and outside pipes of evaporating tank and heater in the sugar factory
CN204874401U (en) Oil -water separation apparatus
CN103062753A (en) Energy-saving blowdown device for industrial boilers
CN202297162U (en) Low temperature pyrogen-free vacuum salt production device
CN207259309U (en) Refining of crude phenol phenol wastewater pre-processing device
CN210944908U (en) Solid waste landfill leachate evaporation crystallization device
CN214634123U (en) Reboiler system optimization structure of ethylene glycol device
CN105036245B (en) A kind of middle temperature biogas slurry waste water tubular type ultrafiltration membrane system processing and reuse technology
CN202175667U (en) Wort continuous treatment device
CN220502971U (en) System for separating stable gasoline by three components of partition tower
CN102627299A (en) Low-temperature heatless vacuum salt making device
CN209791142U (en) Skid-mounted pyrolysis gas separation device
CN214075125U (en) N-formyl morpholine and circulation interval hydrocarbon dehydration system
CN203569043U (en) Purifying plant for tire oil
CN219398987U (en) Circulating heating structure of acetaldehyde tower
CN203625261U (en) Device for removing C3 in ether liquefied gas fractionation process
CN220230169U (en) Steam heat exchange device for heating liquid
CN220250781U (en) Monosodium glutamate crystallization tail gas cooling system
CN216205509U (en) Energy-saving distilled water tank
CN114159820B (en) Energy-saving fractionating device for refining alkylate oil
CN215365629U (en) Negative pressure debenzolization continuous regeneration deslagging device

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant