CN208641808U - A kind of rectifying tower reboiler - Google Patents

A kind of rectifying tower reboiler Download PDF

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Publication number
CN208641808U
CN208641808U CN201821243016.5U CN201821243016U CN208641808U CN 208641808 U CN208641808 U CN 208641808U CN 201821243016 U CN201821243016 U CN 201821243016U CN 208641808 U CN208641808 U CN 208641808U
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CN
China
Prior art keywords
reboiler
steam
controller
inlet
regulating valve
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.)
Expired - Fee Related
Application number
CN201821243016.5U
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Chinese (zh)
Inventor
石宝忠
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.)
Tianjin Shengbo Instrument Co Ltd
Original Assignee
Tianjin Shengbo Instrument 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 Tianjin Shengbo Instrument Co Ltd filed Critical Tianjin Shengbo Instrument Co Ltd
Priority to CN201821243016.5U priority Critical patent/CN208641808U/en
Application granted granted Critical
Publication of CN208641808U publication Critical patent/CN208641808U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The utility model discloses a kind of rectifying tower reboilers, including reboiler ontology, controller, long-distance liquid-level meter, temperature controller, steam-flow meter, water inlet pipe and outlet pipe, inlet, steam (vapor) outlet and discharge port are equipped on reboiler ontology, heater and baffle are equipped in the reboiler ontology, the contact of long-distance liquid-level meter is placed in reboiler body interior cavity, the contact of temperature controller is placed on heater, and the contact of steam-flow meter is placed in inlet;The water inlet pipe is equipped with inlet regulating valve, and outlet pipe is equipped with water regulating valve;The output end of the long-distance liquid-level meter, temperature controller and steam-flow meter is connected with the input terminal of controller respectively;Water regulating valve is connected the output end of controller with inlet regulating valve and out respectively.The utility model can preferably control reboiler liquid level and temperature, to stablize the supply of rectifying column heat, preferably control the operation temperature of rectifying column, guarantee the balance of rectifying column operation and the stabilization of product quality.

Description

A kind of rectifying tower reboiler
Technical field
The utility model belongs to rectifying column technical field, more particularly to a kind of rectifying tower reboiler.
Background technique
Using carbonyl nickel refining, the content of product iron can reach double zero or less ranks, can satisfy downstream high purity nickel The requirement of powder user.In existing production technology, due to rectifying tower structure etc., the equipment such as rectifying column and reboiler were being used Cheng Zhongyi nickel plating, and then block, reboiler is short using the time, influences production efficiency, equipment investment is costly.
Rectifying is that the typical unit operation of mutually soluble liquids mixture is separated in Chemical Manufacture, with Chemical Manufacture and technology The application of development, rectifying column is more and more wider.The capital equipment of distillation process has: rectifying column, reboiler, condenser, return tank etc. Equipment.For rectifying column using feedboard as boundary, top is rectifying section, and lower part is profit reduction and reserving section.The feed liquid of certain temperature and pressure enters essence After evaporating tower, light component is gradually concentrated in rectifying section, all condenses after leaving tower top into return tank, a part is produced as tower top Product, another part are admitted in tower as phegma.And after heavy constituent is concentrated in profit reduction and reserving section, a part is used as bottom product, It is a part of then sent back in tower after reboiler heats, a certain amount of steam air-flow continuously risen is provided for distillation operation.Rectifying column The balance of finance, credits and materials of operation is material balance, vapor liquid equilibrium and heat balance.Rectifying column operation is during control tower balance, and one As control is inlet amount, reflux ratio, the size of heat, cooling capacity.
For reboiler often with rectifying column combined application, reboiler is mounted on rectifier bottoms, passes through reboiler heating tower bottom and steams The liquid for evaporating kettle vaporizes its part and becomes upflowing vapor, is rectifying section, stripping section and the column plate vehicle repair major of rectifying column Heat and mass provides required heat.There is no tower reactor heat supply just without rising steam, it is whole without overhead condensation just without phegma A distillation process just cannot achieve.Most of reboiler is shell-and-tube heat exchanger, and boiling process can occur in shell side, It can occur in tube side, heat medium generallys use steam, is also possible to liquid, gas of heat-carrying etc..
In distillation process, the heat medium steam in Steam reboiler can condense generation condensate liquid, and reboiler liquid level is logical It is controlled frequently with regulating valve.Steam fluctuation will lead to tower bottom liquid temperature fluctuation in reboiler, and the heat balance of rectifying column will be by To influence, and heat balance is material balance and the basis that vapor liquid equilibrium is achieved.
Therefore, how to solve the problems of the above-mentioned prior art becomes the direction of field technical staff effort.
Summary of the invention
The purpose of this utility model is just to provide a kind of rectifying tower reboiler, can be fully solved above-mentioned the deficiencies in the prior art Place.
The purpose of this utility model is realized by following technical proposals: a kind of rectifying tower reboiler, including reboiler Ontology and controller are equipped with inlet, steam (vapor) outlet and discharge port, it is characterised in that: further include long-range on reboiler ontology Liquidometer, temperature controller, steam-flow meter, water inlet pipe and outlet pipe, the reboiler ontology is interior to be equipped with heater and baffle, The contact of long-distance liquid-level meter is placed in reboiler body interior cavity, and the contact of temperature controller is placed on heater, steam stream The contact of meter is placed in inlet;The water inlet pipe is equipped with inlet regulating valve, and outlet pipe is equipped with water regulating valve;It is described The output end of long-distance liquid-level meter, temperature controller and steam-flow meter is connected with the input terminal of controller respectively;Controller it is defeated Water regulating valve is connected outlet with inlet regulating valve and out respectively.
One of it is preferred that, hand-operated valve is additionally provided on outlet pipe, hand-operated valve is disposed in proximity at outlet pipe nozzle.
One of it is preferred that, the discharge port connects a raffinate storage tank by pipeline.
One of it is preferred that, the baffle plate setting is in the position close to discharge port.
One of it is preferred that, connector is equipped on inlet, the connector is flange.
Compared with prior art, the utility model has the beneficial effects that: a kind of rectifying tower reboiler, can preferably control Reboiler liquid level and temperature processed preferably control the operation temperature of rectifying column to stablize the supply of rectifying column heat, guarantee rectifying The balance of tower operation and the stabilization of product quality.
Detailed description of the invention
Fig. 1 is the structure schematic diagram of the utility model.
In attached drawing: reboiler ontology 1, inlet 2, steam (vapor) outlet 3, discharge port 4, raffinate storage tank 5, connection Device 6, heater 7, baffle 8, long-distance liquid-level meter 9, temperature controller 10, steam-flow meter 11, water inlet pipe 12, Outlet pipe 13, inlet regulating valve 14, out water regulating valve 15, hand-operated valve 16.
Specific embodiment
The utility model is further described with attached drawing combined with specific embodiments below.
As shown in Figure 1, in the present embodiment, the reboiler is the Steam reboiler of shell-and-tube, which is set It is placed in the bottom of rectifying column, the shell side that steam enters reboiler provides heat for tower reactor.
A kind of rectifying tower reboiler, including reboiler ontology 1, controller, long-distance liquid-level meter 9, temperature controller 10, steam Flowmeter 11, water inlet pipe 12 and outlet pipe 13.Wherein, controller is computer, belongs to the control equipment in existing rectifying column.Institute It states and is equipped with heater 7 and baffle 8 in reboiler ontology 1, the baffle 8 is disposed in proximity to the position of discharge port 4.In reboiler sheet Body 1 is equipped with inlet 2, steam (vapor) outlet 3 and discharge port 4, and connector 6 is equipped on inlet 2, and the connector 6 is flange, By fixing a connecting tube on connector, the bottom of rectifying column is connected to by connecting tube.The discharge port 4 is connected by pipeline Raffinate is introduced into raffinate storage tank 5 by one raffinate storage tank 5 by discharge port, can also be arranged on the pipeline of discharge port connection Pressure pump reinforces the intensity that raffinate introduces.
The contact of long-distance liquid-level meter 9 is placed in 1 internal cavities of reboiler ontology, and long-distance liquid-level meter 9 passes through computer remote Control, can more preferably, more intuitively control the liquid level of condensate liquid in reboiler.The contact of temperature controller 10 is placed in heater 7 On, temperature controller is controlled remotely by a computer, and can be stablized the supply of rectifying column heat, preferably be controlled the operation of rectifying column Temperature.The contact of steam-flow meter 11 is placed in inlet 2;Steam-flow meter 11 is used to monitor the indifferent gas entered in reboiler The amount of body.The water inlet pipe 12 is equipped with inlet regulating valve 14, and outlet pipe 13 is equipped with water regulating valve 15 and hand-operated valve 16, hand Dynamic valve 16 is disposed in proximity at outlet pipe nozzle.The output of the long-distance liquid-level meter 9, temperature controller 10 and steam-flow meter 11 End is connected with the input terminal of controller respectively;The output end of controller with inlet regulating valve 14 and out 15 phase of water regulating valve respectively Even.
Go out water regulating valve 15 on the inlet regulating valve and outlet pipe on water inlet pipe when the utility model is used, opening With hand-operated valve 16, the valve in air inlet pipe is opened, Self-operated pressure reducing valve is adjusted, is down to pressure after Self-operated pressure reducing valve 0.1MPa opens the valve in air inlet pipe, inert gas is blasted into rectifying column after the completion of driving according to rectifying driving sequence. In use, adjusting the aperture of the valve in air inlet pipe according to service condition, control enters the amount of the inert gas in reboiler, It is monitored simultaneously with steam-flow meter 11.In use, adjusting according to service condition and going out opening for water regulating valve on outlet pipe The amount of hot water in reboiler is flowed out in degree, control.
On the rectifier unit of 150,000 tons of methanol expansion project, due to liquid level in reboiler not easy to control, tower reactor heat It controls bad, seriously affects product quality.Sometimes full liquid level in reboiler, causes liquid hammer, and reboiler shakes;Sometimes in reboiler Aneroid causes valve surge.Using the Steam reboiler of the utility model, preferably the liquid level of condensate liquid in reboiler is carried out Control, tower reactor steam stable, heat are stablized, and reboiler shaking or valve surge phenomenon no longer occur;And also avoid steam All condensation is not directly entered subsequent processing, can be reduced unnecessary waste.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this Made any modifications, equivalent replacements, and improvements etc., should be included in the utility model within the spirit and principle of utility model Protection scope within.

Claims (5)

1. a kind of rectifying tower reboiler, including reboiler ontology and controller are equipped with inlet on reboiler ontology, steam goes out Mouthful and discharge port, it is characterised in that: further include long-distance liquid-level meter, temperature controller, steam-flow meter, water inlet pipe and outlet pipe, Heater and baffle are equipped in the reboiler ontology, the contact of long-distance liquid-level meter is placed in reboiler body interior cavity, temperature The contact of degree controller is placed on heater, and the contact of steam-flow meter is placed in inlet;The water inlet pipe is equipped with water inlet Regulating valve, outlet pipe are equipped with water regulating valve;The output end of the long-distance liquid-level meter, temperature controller and steam-flow meter point It is not connected with the input terminal of controller;Water regulating valve is connected the output end of controller with inlet regulating valve and out respectively.
2. rectifying tower reboiler according to claim 1, it is characterised in that: be additionally provided with hand-operated valve on outlet pipe, manually Valve is disposed in proximity at outlet pipe nozzle.
3. rectifying tower reboiler according to claim 1, it is characterised in that: the discharge port connects a raffinate by pipeline Storage tank.
4. rectifying tower reboiler according to claim 1, it is characterised in that: the baffle plate setting is in the position close to discharge port It sets.
5. rectifying tower reboiler according to claim 1, it is characterised in that: be equipped with connector, the company on inlet Connecing device is flange.
CN201821243016.5U 2018-08-03 2018-08-03 A kind of rectifying tower reboiler Expired - Fee Related CN208641808U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201821243016.5U CN208641808U (en) 2018-08-03 2018-08-03 A kind of rectifying tower reboiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201821243016.5U CN208641808U (en) 2018-08-03 2018-08-03 A kind of rectifying tower reboiler

Publications (1)

Publication Number Publication Date
CN208641808U true CN208641808U (en) 2019-03-26

Family

ID=65787714

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201821243016.5U Expired - Fee Related CN208641808U (en) 2018-08-03 2018-08-03 A kind of rectifying tower reboiler

Country Status (1)

Country Link
CN (1) CN208641808U (en)

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GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190326

Termination date: 20190803