CN213221082U - Energy-saving subsider circulation heating device for alumina production - Google Patents

Energy-saving subsider circulation heating device for alumina production Download PDF

Info

Publication number
CN213221082U
CN213221082U CN202022033138.5U CN202022033138U CN213221082U CN 213221082 U CN213221082 U CN 213221082U CN 202022033138 U CN202022033138 U CN 202022033138U CN 213221082 U CN213221082 U CN 213221082U
Authority
CN
China
Prior art keywords
cell body
pipe
energy
steam coil
saving
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
CN202022033138.5U
Other languages
Chinese (zh)
Inventor
张志勇
方向华
罗登银
张文
王岗
唐勇
冉春
郭晓英
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.)
Chongqing Research Better Science & Technology Co ltd
Original Assignee
Chongqing Research Better Science & Technology 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 Chongqing Research Better Science & Technology Co ltd filed Critical Chongqing Research Better Science & Technology Co ltd
Priority to CN202022033138.5U priority Critical patent/CN213221082U/en
Application granted granted Critical
Publication of CN213221082U publication Critical patent/CN213221082U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

The utility model discloses an energy-saving subsider circulation heating device for alumina production, including the cell body, be provided with inlet pipe, discharging pipe, admission line and the pipeline of giving vent to anger on the cell body, the discharging pipe sets up in the cell body bottom, still includes heater and steam coil, and steam coil sets up and is close to the bottom in the cell body, evenly is provided with the venthole on the steam coil, the air inlet of heater is connected with the intake pipe, intake pipe one end and cell body upper portion intercommunication, and the gas outlet of heater is connected with the circulating line, circulating line and steam coil intercommunication, be provided with separator and fluid-discharge tube on the discharging pipe, the feed inlet and the terminal intercommunication of discharging pipe of separator. The utility model discloses simple structure, convenient operation, the energy saving does benefit to the implementation.

Description

Energy-saving subsider circulation heating device for alumina production
Technical Field
The utility model relates to a heating device, in particular to a settling tank circulating heating device for producing energy-saving aluminum oxide.
Background
The existing aluminum oxide production settling tank for industrial production is fed from the top of the settling tank, and dissolved slurry has heat loss in the conveying process through a feeding pipeline, so that the dissolved slurry needs to be heated when entering the settling tank, the hydrolysis loss of the slurry is reduced, and the yield of aluminum oxide is increased. In the production operation process, steam is conveyed from the upper part of the precipitation tank, the slurry in the settling tank for producing the aluminum oxide is heated at a low speed, the waste of steam energy is caused, a large amount of steam is discharged to the atmosphere through the exhaust funnel, and when the slurry in the settling tank is heated, the upper part is at a high temperature, the lower part is low, the hydrolysis loss of the slurry is large, the yield of the aluminum oxide is reduced, the normal operation of production is influenced, and the production is greatly influenced.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide an energy-saving sedimentation tank circulation heating device for aluminum oxide production, which has simple structure, convenient operation and energy saving.
In order to achieve the above purpose, the utility model adopts the technical scheme that: the utility model discloses an energy-saving subsider circulation heating device for alumina production, including the cell body, be provided with inlet pipe, discharging pipe, admission line and the pipeline of giving vent to anger on the cell body, the discharging pipe sets up in the cell body bottom, still includes heater and steam coil, and steam coil sets up and is close to the bottom in the cell body, evenly is provided with the venthole on the steam coil, the air inlet of heater is connected with the intake pipe, intake pipe one end and cell body upper portion intercommunication, and the gas outlet of heater is connected with the circulating line, circulating line and steam coil intercommunication, be provided with separator and fluid-discharge tube on the discharging pipe, the feed inlet and the terminal intercommunication of discharging.
Preferably, the discharge port of the separator is provided with a valve.
Preferably, the liquid discharge pipe is arranged perpendicular to the discharge pipe.
Compared with the prior art, the utility model has the advantages of: the utility model has simple structure and convenient operation, and is provided with the heater which can circularly heat the gas in the settling tank, thereby saving energy; set up the steam coil who evenly takes out the gas pocket in the lower part of subsider for the thick liquids heating is abundant in the subsider, and it is fast to heat up, reduces steam and arranges to atmospheric loss, practices thrift the steam quantity, practices thrift heat energy, reduces the alumina hydrolysis loss, increases alumina output, sets up separator and fluid-discharge tube on the discharging pipe, is convenient for separate alumina, does benefit to the implementation.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Detailed Description
The present invention will be further explained with reference to the accompanying drawings.
Referring to fig. 1, the energy-saving sedimentation tank circulation heating device for aluminum oxide production of the utility model comprises a tank body 1, wherein the tank body 1 is provided with a feed pipe 2, a discharge pipe 3, an air inlet pipe 4 and an air outlet pipe 5, the discharge pipe 3 is arranged at the bottom of the tank body 1, the sedimentation tank circulation heating device also comprises a heater 6 and a steam coil pipe 9, the steam coil pipe 9 is arranged in the tank body 1 and is close to the bottom, the steam coil pipe 9 is uniformly provided with air outlet holes 10, an air inlet pipe 7 is connected to an air inlet of the heater 6, one end of the air inlet pipe 7 is communicated with the upper part of the tank body 1, an air outlet of the heater 6 is connected with a circulating pipeline 8, the circulating pipeline 8 is communicated with a steam coil pipe 9, a separator 11 and a liquid discharge pipe 12 are arranged on the discharge pipe 3, a feed inlet of the separator 11 is communicated with the tail end of the discharge pipe 3, a valve 13 is arranged at the discharge hole of the separator 11, and the discharge pipe 12 is perpendicular to the discharge pipe 3.
During the use, the raw materials gets into in the cell body 1 from inlet pipe 2, steam gets into from 7 says 4 intake pipe, set up heater 6, can be to the steam cycle heating in the cell body 1, the energy saving, set up the steam coil pipe 9 of evenly taking out gas pocket 10 in the lower part of cell body 1, make the thick liquid heating of material in the subsider abundant, it is fast to heat up, reduce steam and arrange atmospheric loss, practice thrift the steam quantity, set up separator 11 and fluid-discharge tube 12 on discharging pipe 3, be convenient for separate aluminium oxide. The utility model discloses simple structure, convenient operation practices thrift heat energy, does benefit to the implementation.

Claims (3)

1. The utility model provides an energy-saving subsider circulation heating device for alumina production, includes the cell body, is provided with inlet pipe, discharging pipe, admission line and the pipeline of giving vent to anger on the cell body, and the discharging pipe sets up in the cell body bottom, its characterized in that: still include heater and steam coil, steam coil sets up and is close to the bottom in the cell body, evenly is provided with the venthole on the steam coil, the air inlet of heater is connected with the intake pipe, intake pipe one end and cell body upper portion intercommunication, and the gas outlet of heater is connected with circulating line, and circulating line and steam coil intercommunication are provided with separator and fluid-discharge tube on the discharging pipe, the feed inlet of separator and the terminal intercommunication of discharging pipe.
2. The energy-saving sedimentation tank circulation heating device for aluminum oxide production according to claim 1, characterized in that: and a valve is arranged at a discharge hole of the separator.
3. The energy-saving sedimentation tank circulation heating device for aluminum oxide production according to claim 1, characterized in that: the liquid discharge pipe is perpendicular to the discharge pipe.
CN202022033138.5U 2020-09-17 2020-09-17 Energy-saving subsider circulation heating device for alumina production Active CN213221082U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202022033138.5U CN213221082U (en) 2020-09-17 2020-09-17 Energy-saving subsider circulation heating device for alumina production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202022033138.5U CN213221082U (en) 2020-09-17 2020-09-17 Energy-saving subsider circulation heating device for alumina production

Publications (1)

Publication Number Publication Date
CN213221082U true CN213221082U (en) 2021-05-18

Family

ID=75874017

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202022033138.5U Active CN213221082U (en) 2020-09-17 2020-09-17 Energy-saving subsider circulation heating device for alumina production

Country Status (1)

Country Link
CN (1) CN213221082U (en)

Similar Documents

Publication Publication Date Title
CN213221082U (en) Energy-saving subsider circulation heating device for alumina production
CN201372257Y (en) Device for continuously cracking organic glass to regenerate methyl methacrylate
CN106190811A (en) A kind of diphasic anaerobic fermentation is from stirring reaction unit
CN204356320U (en) A kind of biomass steam blasting assembly
CN204803247U (en) Formaldehyde preparation device of methyl alcohol direct boiling
CN205351987U (en) Brush silk raw materials vacuum drying machine
CN211864987U (en) Continuous efficient oxidation reactor
CN217052344U (en) Vacuum continuous concentration device for rare earth feed liquid
CN206843089U (en) A kind of modified alumina producing sedimentation tank heater
CN208980736U (en) Reactor tank is used in a kind of processing of citric acid complex enzyme
CN208562380U (en) A kind of dry anaerobic fermentation tank for biogas reaction
CN112047761A (en) Non-water-flushing excrement collecting and fermenting device and fermenting process thereof
CN214666090U (en) Energy-saving catalyst kiln
CN2839282Y (en) The waste heat recovery tower
CN203316124U (en) Organic silicon adhesive production line
CN201169578Y (en) Heating ammonia charging apparatus in o-tolunitrile production
CN217715977U (en) Electrode paste waste heat utilization device
CN220649127U (en) Graphitizing furnace for energy-saving lithium battery cathode material
CN216395281U (en) Low-temperature negative-pressure concentration equipment
CN216205120U (en) Device for reducing steam consumption by recycling dry waste heat
CN213652228U (en) Novel heat exchange cyclone desanding device
CN201424466Y (en) Vacuum flash evaporation cooling device for beer saccharifying section
CN202754926U (en) Series combination high-temperature conduction oil heating reaction still
CN214232930U (en) Pneumatic filter pressing equipment
CN215628221U (en) Be used for energy-efficient apparatus for producing of manganese silicon alloy

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant