CN202938280U - Magnesium smelting reducing slag heat recovery boiler - Google Patents

Magnesium smelting reducing slag heat recovery boiler Download PDF

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Publication number
CN202938280U
CN202938280U CN2012206772632U CN201220677263U CN202938280U CN 202938280 U CN202938280 U CN 202938280U CN 2012206772632 U CN2012206772632 U CN 2012206772632U CN 201220677263 U CN201220677263 U CN 201220677263U CN 202938280 U CN202938280 U CN 202938280U
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CN
China
Prior art keywords
barrel body
cylinder body
outer cylinder
reducing slag
inner barrel
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.)
Withdrawn - After Issue
Application number
CN2012206772632U
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Chinese (zh)
Inventor
张少军
杨沛胥
张伟东
雷振华
周寿山
刘刚
李荣斌
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Kaitai Magnesium Co ltd
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Kaitai Magnesium Co ltd
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Priority to CN2012206772632U priority Critical patent/CN202938280U/en
Application granted granted Critical
Publication of CN202938280U publication Critical patent/CN202938280U/en
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    • 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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The utility model relates to a heat recovery boiler, in particular to a magnesium smelting reducing slag heat recovery boiler recovering high-temperature waste slag energy produced at magnesium metal hot-method manufacturing time. The magnesium smelting reducing slag heat recovery boiler comprises an outer barrel body, an inner barrel body, end sockets at two ends of the outer barrel body, an edge pulling pipe plate at one end of the inner barrel body and a sealing plate at the other end of the inner barrel body. The magnesium smelting reducing slag heat recovery boiler is characterized in that a cooling water inlet is formed in one side end socket, a heat exchange tube bundle is horizontally fixed inside the inner barrel body through the sealing plate and a supporting plate, a high-temperature waste slag inlet and a low-temperature waste slag outlet are arranged at the top and the bottom of the outer barrel body at intervals, an exhaust port, a pressure meter port, a safety valve port, a lifting lug, and a high-temperature water outlet are sequentially arranged on the upper portion of the outer barrel body from left to right, and a sewage drainage port and a saddle seat are sequentially arranged on the lower portion of the outer barrel body from right to left. The magnesium smelting reducing slag heat recovery boiler is unique in structure, utilizes high-temperature waste slag as an energy resource to heat cooling water into high-temperature water, realizes recycle of energy, saves a large amount of fossil energy, and reduces production cost of magnesium metal.

Description

Magnesium smelting reducing slag waste heat boiler
Technical field
The utility model relates to a kind of waste heat boiler, especially relates to a kind of magnesium smelting reducing slag waste heat boiler that reclaims the high temperature waste residue energy that produces when hot legal system is got magnesium metal.
Background technology
At present China is sure to occupy the first in the world large magnesium producing country and exporting country, and the production of magnesium metal mainly contains two kinds of thermal reduction and electrolysis, but the most enterprises of China use thermal reduction legal system magnesium technique.Due to the magnesium-reduced slag of 6 tons of 1 ton of magnesium average generation of the every production of method for smelting magnesium by hot, and the temperature that slag leaves the reduction tank is the high temperature of 1200 ℃, contained a large amount of heat energy.But be subject to existing technology, high temperature furnace slag directly is transported to be put plant area aside as useless and piles up and be difficult to effective utilization, and the UTILIZATION OF VESIDUAL HEAT IN that high temperature furnace slag is contained more rarely has research to use.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, the high temperature waste residue that provide a kind of structure uniqueness, utilizes method for smelting magnesium by hot to produce is heated as high-temperature water to cooling water as energy source, realized the recycling of energy, save a large amount of fossil energies, reduced the magnesium smelting reducing slag waste heat boiler of the production cost of magnesium metal.
The utility model is realized in the following way:
a kind of magnesium smelting reducing slag waste heat boiler, it comprises outer cylinder body, inner barrel, the end socket at outer cylinder body two ends, the shrouding of pulling limit tube sheet and the other end of inner barrel one end, it is characterized in that: open on an above-mentioned side seal head cooling water inlet, heat-exchanging tube bundle is horizontally fixed on inside above-mentioned inner barrel by shrouding and gripper shoe, high temperature waste residue entrance and low temperature waste residue outlet disposed at equal distance are in top and the bottom of outer cylinder body, exhaust outlet is equipped with on outer cylinder body top from left to right successively, pressure gauge connection, relief valve connection, hanger, the high-temperature water outlet, the outer cylinder body bottom is equipped with sewage draining exit and saddle from right to left successively,
Be fixed with vertical clapboard and horizontal baffle on described gripper shoe;
Be provided with population on the end socket of the both sides of described outer cylinder body, population is provided with hand hole, and the steam discharge base is housed on described exhaust outlet;
Distance between described heat-exchanging tube bundle can make the high temperature pelletizing pass through smoothly.
The utility model has following effect:
1) structure is unique: it comprises outer cylinder body the waste heat boiler that the utility model provides, inner barrel, the end socket at outer cylinder body two ends, the shrouding of pulling limit tube sheet and the other end of inner barrel one end, it is characterized in that: open on an above-mentioned side seal head cooling water inlet, heat-exchanging tube bundle is horizontally fixed on inside above-mentioned inner barrel by shrouding and gripper shoe, high temperature waste residue entrance and low temperature waste residue outlet disposed at equal distance are in top and the bottom of outer cylinder body, exhaust outlet is equipped with on outer cylinder body top from left to right successively, pressure gauge connection, relief valve connection, hanger, the high-temperature water outlet, the outer cylinder body bottom is equipped with sewage draining exit and saddle from right to left successively, heat exchanger tube is horizontally fixed on the inner barrel the inside by the shrouding in the end socket of waste heat boiler two ends and gripper shoe, and the distance between tube bank can make the high temperature pelletizing pass through smoothly, cooling water is exported for the user by the high-temperature water outlet after being heated as high-temperature water by the high temperature waste residue, high temperature waste residue entrance and low temperature waste residue outlet disposed at equal distance are in waste heat boiler top and bottom, and entering and discharging of waste residue is convenient in its position correspondence one by one.
2) the high temperature waste residue that utilizes method for smelting magnesium by hot to produce is heated as high-temperature water to cooling water as energy source, realized the recycling of energy: the waste heat boiler low-temperature cooling water that the utility model provides is flowed in waste heat boiler one side seal head by the cooling water inlet, heating is proceeded in the gap that the heating of carrying out four backhauls by heat exchanger tube flows between inner barrel and outer cylinder body afterwards, and final cooling water is heated to be high-temperature steam and is exported by steam (vapor) outlet; The high temperature waste residue is put into successively waste heat boiler by high temperature waste residue entrance by certain time interval cooling water is heated, and completes to open the outlet of low temperature waste residue after the heat exchange of one-period and discharge waste residue after being cooled.The Conversion of Energy that the high temperature waste residue that it can effectively produce the magnesium smelting contains is steam, for other equipment provide kinetic energy.
3) improve workman's work situation, reduce workman's labour intensity: be down to 200 ℃ because the utility model can make the high temperature waste residue of 1200 ℃, so most waste heats of high temperature waste residue all are recovered utilization.By calculating, the energy equivalence that the high temperature waste residue that one ton of magnesium metal of every production produces discharges in cooling procedure is in the energy of 150kg standard coal, use the utility model not only can save a lot of fossil fuels, can also reduce the discharging of a large amount of dust, improve workman's work situation, reduce workman's labour intensity.
Description of drawings
Fig. 1 is front view of the present utility model;
Fig. 2 is the A-A cutaway view in the utility model Fig. 1;
Fig. 3 is left view of the present utility model.
The specific embodiment
a kind of magnesium smelting reducing slag waste heat boiler, it comprises outer cylinder body 9, inner barrel 10, the end socket 2 at outer cylinder body 9 two ends, the shrouding of pulling limit tube sheet 3 and the other end 12 of inner barrel 10 1 ends, as shown in Figure 1: open on an above-mentioned side seal head 2 cooling water inlet 1, heat-exchanging tube bundle 16 is horizontally fixed on above-mentioned inner barrel 10 the insides by shrouding 12 and gripper shoe 17, high temperature waste residue entrance 8 and low temperature waste residue outlet 15 disposed at equal distance are in top and the bottom of outer cylinder body 9, exhaust outlet 4 is equipped with on outer cylinder body 9 tops from left to right successively, pressure gauge connection 5, relief valve connection 6, hanger 7, high-temperature water outlet 11, outer cylinder body 9 bottoms are equipped with sewage draining exit 13 and saddle 14 from right to left successively,
As shown in Figure 2: be fixed with vertical clapboard 18 and horizontal baffle 19 on described gripper shoe 17;
As shown in Figure 3: be provided with population 22 on the both sides of described outer cylinder body 9 end socket 2, population 22 is provided with hand hole 20, on described exhaust outlet 4, steam discharge base 21 is housed;
Distance between described heat-exchanging tube bundle 16 can make the high temperature pelletizing pass through smoothly.
Low-temperature cooling water is flowed in waste heat boiler one side seal head 2 by cooling water inlet 1, heating is proceeded in the gap that the heating of carrying out four backhauls by heat exchanger tube 16 flows between inner barrel 10 and outer cylinder body 9 afterwards, and final cooling water is heated to be high-temperature steam by steam (vapor) outlet 11 outputs; The high temperature waste residue is put into successively waste heat boiler by high temperature waste residue entrance 8 by certain time interval cooling water is heated, and opens the waste residues that low temperature waste residue outlet 15 is discharged after being cooled after completing the heat exchange of one-period.The Conversion of Energy that the high temperature waste residue that it can effectively produce the magnesium smelting contains is steam, for other equipment provide kinetic energy.

Claims (4)

1. magnesium smelting reducing slag waste heat boiler, it comprises outer cylinder body (9), inner barrel (10), the end socket (2) at outer cylinder body (9) two ends, the shrouding (12) of pulling limit tube sheet (3) and the other end of inner barrel (10) one ends, it is characterized in that: open on an above-mentioned side seal head (2) cooling water inlet (1), heat-exchanging tube bundle (16) is horizontally fixed on inside above-mentioned inner barrel (10) by shrouding (12) and gripper shoe (17), high temperature waste residue entrance (8) and low temperature waste residue outlet (15) disposed at equal distance are in top and the bottom of outer cylinder body (9), exhaust outlet (4) is equipped with on outer cylinder body (9) top from left to right successively, pressure gauge connection (5), relief valve connection (6), hanger (7), high-temperature water outlet (11), outer cylinder body (9) bottom is equipped with sewage draining exit (13) and saddle (14) from right to left successively.
2. magnesium smelting reducing slag waste heat boiler as claimed in claim 1, is characterized in that: be fixed with vertical clapboard (18) and horizontal baffle (19) on described gripper shoe (17).
3. magnesium smelting reducing slag waste heat boiler as claimed in claim 1, it is characterized in that: be provided with population (22) on the both sides end socket (2) of described outer cylinder body (9), population (22) is provided with hand hole (20), and steam discharge base (21) is housed on described exhaust outlet (4).
4. magnesium smelting reducing slag waste heat boiler as claimed in claim 1, it is characterized in that: the distance between described heat-exchanging tube bundle (16) can make the high temperature pelletizing pass through smoothly.
CN2012206772632U 2012-12-11 2012-12-11 Magnesium smelting reducing slag heat recovery boiler Withdrawn - After Issue CN202938280U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2012206772632U CN202938280U (en) 2012-12-11 2012-12-11 Magnesium smelting reducing slag heat recovery boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2012206772632U CN202938280U (en) 2012-12-11 2012-12-11 Magnesium smelting reducing slag heat recovery boiler

Publications (1)

Publication Number Publication Date
CN202938280U true CN202938280U (en) 2013-05-15

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CN2012206772632U Withdrawn - After Issue CN202938280U (en) 2012-12-11 2012-12-11 Magnesium smelting reducing slag heat recovery boiler

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CN (1) CN202938280U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102966934A (en) * 2012-12-11 2013-03-13 开泰镁业有限公司 magnesium smelting reducing slag waste heat boiler

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102966934A (en) * 2012-12-11 2013-03-13 开泰镁业有限公司 magnesium smelting reducing slag waste heat boiler
CN102966934B (en) * 2012-12-11 2014-10-29 西安交通大学 Magnesium smelting reducing slag waste heat boiler

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C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20130515

Effective date of abandoning: 20141029

RGAV Abandon patent right to avoid regrant