CN204165379U - Lead anode slurry smelting furnace - Google Patents

Lead anode slurry smelting furnace Download PDF

Info

Publication number
CN204165379U
CN204165379U CN201420558680.4U CN201420558680U CN204165379U CN 204165379 U CN204165379 U CN 204165379U CN 201420558680 U CN201420558680 U CN 201420558680U CN 204165379 U CN204165379 U CN 204165379U
Authority
CN
China
Prior art keywords
smoke pipe
unicom
row smoke
row
pipe
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
CN201420558680.4U
Other languages
Chinese (zh)
Inventor
曹彦富
唐承伟
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.)
HUNAN XINGGUANG NONFERROUS METAL Co Ltd
Original Assignee
HUNAN XINGGUANG NONFERROUS METAL 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 HUNAN XINGGUANG NONFERROUS METAL Co Ltd filed Critical HUNAN XINGGUANG NONFERROUS METAL Co Ltd
Priority to CN201420558680.4U priority Critical patent/CN204165379U/en
Application granted granted Critical
Publication of CN204165379U publication Critical patent/CN204165379U/en
Expired - Fee Related 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Vertical, Hearth, Or Arc Furnaces (AREA)

Abstract

The utility model discloses a kind of lead anode slurry smelting furnace, comprise reverberatory furnace, also comprise smoke collecting device, smoke collecting device comprises first row smoke pipe, the first collector, second row smoke pipe and the second collector, first row smoke pipe in or M or N or W or V-type, this first row smoke pipe arrival end is provided with valve and with reverberatory furnace inner top UNICOM, the port of export by air-introduced machine and discharge region UNICOM; First collector be positioned at bottom first row smoke pipe or M or N or W or V-type corner and with first row smoke pipe UNICOM, make the first collector can collect solid matter in first row smoke pipe; Second row smoke pipe in or M or N or W or V-type, this second row smoke pipe arrival end and reverberatory furnace inner top UNICOM, the port of export are by air-introduced machine and discharge region UNICOM; Second collector be positioned at bottom second row smoke pipe or M or N or W or V corner and with second row smoke pipe UNICOM, make the second collector can collect solid matter in second row smoke pipe.The As and Sb separation contained in lead anode slurry is collected, and purity is high, and quality is good.

Description

Lead anode slurry smelting furnace
Technical field
The utility model relates to a kind of smelting furnace, particularly a kind of lead anode slurry smelting furnace.
Background technology
Lead anode slurry process generally adopts traditional pyrogenic attack technique, utilizes the volatile characteristic of the arsenic in lead anode slurry in composition, antimony, arsenic, antimony to be volatilized from lead anode slurry and separates, discharged, then collected by gathering-device by smoke exhaust pipe by high temperature.At present by arsenic, antimony from lead anode slurry volatile matter from smelting furnace, its smoke exhaust pipe adopts one by the arsenic in lead anode slurry, antimony flue gas dual disposal, what namely gathering-device was collected is the mixture of arsenic particle, antimony particle, cause in antimony particle containing a large amount of arsenic particles, antimony purity is low, cause price low, economic benefit is low, inconvenient.
Utility model content
The technical problem that the utility model solves is to provide a kind of arsenic, antimony flue gas separated and collected, purity high lead anode slurry smelting furnace easy to use.
In order to solve the problems of the technologies described above, lead anode slurry smelting furnace of the present utility model, comprise reverberatory furnace, also comprise smoke collecting device, described smoke collecting device comprises first row smoke pipe, the first collector, second row smoke pipe and the second collector, described first row smoke pipe in or M or N or W or V-type, this first row smoke pipe arrival end is provided with valve and with reverberatory furnace inner top UNICOM, the port of export by air-introduced machine and discharge region UNICOM; Described first collector be positioned at bottom first row smoke pipe or M or N or W or V-type corner and with first row smoke pipe UNICOM, make the first collector can collect solid matter in first row smoke pipe; Described second row smoke pipe in or M or N or W or V-type, this second row smoke pipe arrival end and reverberatory furnace inner top UNICOM, the port of export are by air-introduced machine and discharge region UNICOM; Described second collector be positioned at bottom second row smoke pipe or M or N or W or V corner and with second row smoke pipe UNICOM, make the second collector can collect solid matter in second row smoke pipe.
Also include smoke pipe and enter cigarette threeway; Described enter smoke pipe one end and reverberatory furnace inner top UNICOM, the other end and enter a cigarette threeway wherein mouth UNICOM of UNICOM; Described enter cigarette threeway Ling Liang UNICOM mouth respectively with first row smoke pipe arrival end, second row smoke pipe arrival end UNICOM; Make first row smoke pipe arrival end, second row smoke pipe arrival end passes through into cigarette threeway, enters smoke pipe and reverberatory furnace inner top UNICOM.
Also comprise pipe and smoke threeway; The described pipe port of export is by air-introduced machine and discharge region UNICOM, an arrival end and smoke threeway wherein mouth UNICOM of UNICOM; Described smoke threeway Ling Liang UNICOM mouth respectively with the first row smoke pipe port of export, second row smoke pipe port of export UNICOM; Make the first row smoke pipe port of export, the second row smoke pipe port of export by smoke threeway, pipe, air-introduced machine and discharge region UNICOM.
Also comprise cooling circulation water tank, the water inlet of described cooling circulation water tank by pipeline and cistern UNICOM by pump and cistern UNICOM, delivery port, is made the water in cistern be pumped into after in cooling circulation water tank by pump and is thrown in cistern by delivery port again; The port of export of described first row smoke pipe, second row smoke pipe is each passed through cooling circulation water tank and discharge region UNICOM, makes first row smoke pipe, second row smoke pipe by the water cooling cooling in cooling circulation water tank.
Adopt structure of the present utility model, owing to also comprising smoke collecting device, described smoke collecting device comprises first row smoke pipe, the first collector, second row smoke pipe and the second collector.The volatilization temperature of arsenic is 200-900 DEG C, and the volatilization temperature of antimony is 900-1800 DEG C, and the volatilization temperature of arsenic is lower than the volatilization temperature of antimony.During use, first open the valve of first row smoke pipe or second row smoke pipe, when the temperature in reverberatory furnace is 200-900 DEG C, the arsenic volatilization contained in lead anode slurry forms gaseous state arsenic, gaseous state arsenic discharged by first row smoke pipe or second row smoke pipe and simultaneously in first row smoke pipe or second row smoke pipe cooling form arsenic particle and collected by the first collector or the second collector.After the arsenic volatilization regular hour, close the valve of first row smoke pipe or second row smoke pipe, open the valve of second row smoke pipe or first row smoke pipe simultaneously, temperature in reverberatory furnace is continued to heat up, the temperature in reverberatory furnace is made to reach 900-1800 DEG C, to meet the volatilization temperature of antimony, the antimony formation gaseous state antimony contained in lead anode slurry, gaseous state antimony is discharged by second row smoke pipe or first row smoke pipe and in second row smoke pipe or first row smoke pipe, is cooled formation antimony particle simultaneously and collected by the second collector or the first collector.The As and Sb separation contained in lead anode slurry is collected, and purity is high, and quality is good, and high financial profit is simple to operate, easy to use.
Again owing to also including smoke pipe and entering cigarette threeway; Described enter smoke pipe one end and reverberatory furnace inner top UNICOM, the other end and enter a cigarette threeway wherein mouth UNICOM of UNICOM; Described enter cigarette threeway Ling Liang UNICOM mouth respectively with first row smoke pipe arrival end, second row smoke pipe arrival end UNICOM; Make first row smoke pipe arrival end, second row smoke pipe arrival end passes through into cigarette threeway, enters smoke pipe and reverberatory furnace inner top UNICOM.When building reverberatory furnace, first row smoke pipe arrival end, second row smoke pipe arrival end pass through into cigarette threeway, enter smoke pipe and reverberatory furnace inner top UNICOM, and construct more convenient, cost is lower, operates simpler.
Again owing to also comprising pipe and smoke threeway; The described pipe port of export is by air-introduced machine and discharge region UNICOM, an arrival end and smoke threeway wherein mouth UNICOM of UNICOM; Described smoke threeway Ling Liang UNICOM mouth respectively with the first row smoke pipe port of export, second row smoke pipe port of export UNICOM; Make the first row smoke pipe port of export, the second row smoke pipe port of export by smoke threeway, pipe, air-introduced machine and discharge region UNICOM.The first row smoke pipe port of export, the second row smoke pipe port of export are by smoke threeway, pipe and same air-introduced machine UNICOM, and cost is lower, management, more convenient operation.
Owing to also comprising cooling circulation water tank, the water inlet of described cooling circulation water tank by pipeline and cistern UNICOM by pump and cistern UNICOM, delivery port, is made the water in cistern be pumped into after in cooling circulation water tank by pump and is thrown in cistern by delivery port again; The port of export of described first row smoke pipe, second row smoke pipe is each passed through cooling circulation water tank and discharge region UNICOM, makes first row smoke pipe, second row smoke pipe by the water cooling cooling in cooling circulation water tank.During use, first row smoke pipe, second row smoke pipe are by the water cooling cooling in cooling circulation water tank, and the cooling effect of first row smoke pipe, second row smoke pipe is better, and namely the speed of gaseous state arsenic, gaseous state antimony cooling formation particle is faster, use more convenient, use cost is lower.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the utility model is described in detail:
As shown in Figure 1, lead anode slurry smelting furnace of the present utility model, comprises reverberatory furnace 10, also comprises smoke collecting device.Smoke collecting device comprises first row smoke pipe 3, first collector 7, second row smoke pipe 9 and the second collector 8.First row smoke pipe 3 is in N-type.First row smoke pipe 3 also can be M type, W type, V-type.This first row smoke pipe 3 arrival end is provided with valve and with reverberatory furnace 10 inner top UNICOM, the port of export by air-introduced machine 5 and discharge region UNICOM.First collector 7 be positioned at N-type corner bottom first row smoke pipe 3 and with first row smoke pipe 3 UNICOM, make the first collector 7 can collect solid matter in first row smoke pipe 3.Second row smoke pipe 9 is in N-type.Second row smoke pipe 9 also can be M type, W type, V-type.This second row smoke pipe 9 arrival end and reverberatory furnace 10 inner top UNICOM, the port of export are by air-introduced machine and discharge region UNICOM.Second collector 8 be positioned at bottom second row smoke pipe 9 or M or N or W or V-type corner and with second row smoke pipe 9 UNICOM, make the second collector 8 can collect solid matter in second row smoke pipe 9.
In order to make cost lower, operate simpler.Also include smoke pipe 1 and enter cigarette threeway 2.Enter smoke pipe 1 one end and reverberatory furnace 10 inner top UNICOM, the other end and enter a cigarette threeway 2 wherein mouth UNICOM of UNICOM.Enter cigarette threeway 2 Ling Liang UNICOM mouth respectively with first row smoke pipe 3 arrival end, second row smoke pipe 9 arrival end UNICOM.Make first row smoke pipe 3 arrival end, second row smoke pipe 9 arrival end passes through into cigarette threeway 2, enters smoke pipe 1 and reverberatory furnace 10 inner top UNICOM.When building reverberatory furnace, first row smoke pipe arrival end, second row smoke pipe arrival end pass through into cigarette threeway, enter smoke pipe and reverberatory furnace inner top UNICOM, and construct more convenient, cost is lower, operates simpler.
In order to make cost lower, management, more convenient operation.Also comprise pipe and smoke threeway 6.The pipe port of export is by air-introduced machine 5 and discharge region UNICOM, arrival end and a smoke threeway 6 wherein mouth UNICOM of UNICOM.Smoke threeway 6 Ling Liang UNICOM mouth respectively with first row smoke pipe 3 port of export, second row smoke pipe 9 port of export UNICOM.Make first row smoke pipe 3 port of export, second row smoke pipe 9 port of export by smoke threeway 6, pipe, air-introduced machine 5 and discharge region UNICOM.The first row smoke pipe port of export, the second row smoke pipe port of export are by smoke threeway, pipe and same air-introduced machine UNICOM, and cost is lower, management, more convenient operation.
Cool the speed forming particle to make gaseous state arsenic, gaseous state antimony faster, use more convenient, use cost is lower.Also comprise cooling circulation water tank 4, the water inlet of described cooling circulation water tank 4 by pipeline and cistern UNICOM by pump and cistern UNICOM, delivery port, is made the water in cistern be pumped into after in cooling circulation water tank 4 by pump and is thrown in cistern by delivery port.The port of export of first row smoke pipe 3, second row smoke pipe 9 is each passed through cooling circulation water tank 4 and discharge region UNICOM, makes first row smoke pipe 3, second row smoke pipe 9 by the water cooling cooling in cooling circulation water tank 4.During use, first row smoke pipe, second row smoke pipe are by the water cooling cooling in cooling circulation water tank, and the cooling effect of first row smoke pipe, second row smoke pipe is better, and namely the speed of gaseous state arsenic, gaseous state antimony cooling formation particle is faster, use more convenient, use cost is lower.

Claims (4)

1. a lead anode slurry smelting furnace, comprise reverberatory furnace (10), it is characterized in that: also comprise smoke collecting device, described smoke collecting device comprises first row smoke pipe (3), the first collector (7), second row smoke pipe (9) and the second collector (8), described first row smoke pipe (3) in or M or N or W or V-type, this first row smoke pipe (3) arrival end is provided with valve and with reverberatory furnace (10) inner top UNICOM, the port of export by air-introduced machine (5) and discharge region UNICOM; Described first collector (7) be positioned at first row smoke pipe (3) bottom or M or N or W or V-type corner and with first row smoke pipe (3) UNICOM, make the first collector (7) that solid matter in first row smoke pipe (3) can be collected; Described second row smoke pipe (9) in or M or N or W or V-type, this second row smoke pipe (9) arrival end and reverberatory furnace (10) inner top UNICOM, the port of export are by air-introduced machine and discharge region UNICOM; Described second collector (8) be positioned at second row smoke pipe (9) bottom or M or N or W or V-type corner and with second row smoke pipe (9) UNICOM, make the second collector (8) that solid matter in second row smoke pipe (9) can be collected.
2. lead anode slurry smelting furnace according to claim 1, is characterized in that: also include smoke pipe (1) and enter cigarette threeway (2); Described enter smoke pipe (1) one end and reverberatory furnace (10) inner top UNICOM, the other end and enter cigarette threeway (2) wherein mouth UNICOM of UNICOM; Described enter cigarette threeway (2) Ling Liang UNICOM mouth respectively with first row smoke pipe (3) arrival end, second row smoke pipe (9) arrival end UNICOM; Make first row smoke pipe (3) arrival end, second row smoke pipe (9) arrival end passes through into cigarette threeway (2), enters smoke pipe (1) and reverberatory furnace (10) inner top UNICOM.
3. lead anode slurry smelting furnace according to claim 1, is characterized in that: also comprise pipe and smoke threeway (6); The described pipe port of export is by air-introduced machine (5) and discharge region UNICOM, arrival end and smoke threeway (6) wherein mouth UNICOM of UNICOM; Described smoke threeway (6) Ling Liang UNICOM mouth respectively with first row smoke pipe (3) port of export, second row smoke pipe (9) port of export UNICOM; Make first row smoke pipe (3) port of export, second row smoke pipe (9) port of export by smoke threeway (6), pipe, air-introduced machine (5) and discharge region UNICOM.
4. lead anode slurry smelting furnace according to claim 1, it is characterized in that: also comprise cooling circulation water tank (4), the water inlet of described cooling circulation water tank (4) by pipeline and cistern UNICOM by pump and cistern UNICOM, delivery port, is made the water in cistern be pumped into after in cooling circulation water tank (4) by pump and is thrown in cistern by delivery port again; The port of export of described first row smoke pipe (3), second row smoke pipe (9) is each passed through cooling circulation water tank (4) and discharge region UNICOM, makes first row smoke pipe (3), second row smoke pipe (9) by the water cooling cooling in cooling circulation water tank (4).
CN201420558680.4U 2014-09-26 2014-09-26 Lead anode slurry smelting furnace Expired - Fee Related CN204165379U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420558680.4U CN204165379U (en) 2014-09-26 2014-09-26 Lead anode slurry smelting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420558680.4U CN204165379U (en) 2014-09-26 2014-09-26 Lead anode slurry smelting furnace

Publications (1)

Publication Number Publication Date
CN204165379U true CN204165379U (en) 2015-02-18

Family

ID=52539061

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420558680.4U Expired - Fee Related CN204165379U (en) 2014-09-26 2014-09-26 Lead anode slurry smelting furnace

Country Status (1)

Country Link
CN (1) CN204165379U (en)

Similar Documents

Publication Publication Date Title
CN203128593U (en) Efficient blast furnace slag-washing water waste heat recycling system adopting INBA process
CN201680399U (en) Combustion-supporting device for membrane separation oxygen generation
CN204165379U (en) Lead anode slurry smelting furnace
CN203128597U (en) Efficient blast furnace slag-washing water waste heat recycling system adopting mintel process
CN203128596U (en) Efficient blast furnace slag-washing water waste heat recycling system adopting bottom-filtration process
CN207405220U (en) A kind of sensing zinc dust distillation stove
CN206334513U (en) Flue gas takes off white device
CN207402110U (en) A kind of plating cadmia melting continuously zinc powder furnace
CN204911206U (en) Rare earth metal smelts tail gas recovery unit
CN204555655U (en) A kind of environment-friendly type air blast smelting furnace
CN203728903U (en) Leaching system for preparing vanadium solution by quenching roasting clinker of vanadium slag
CN109780876A (en) Lead anode slurry smelting furnace
CN205269297U (en) Exhaust gas purification system in retreatment of tombarthite phosphor powder waste material
CN204535432U (en) Cement plant kiln hood who knows cooling machine low-temperature flue gas residual neat recovering system
CN207294647U (en) A kind of plasticizer esterification device
CN204320007U (en) A kind of high-temperature flue gas purification equipment of biomass boiler
CN204063748U (en) A kind of film concentrates cooling system
CN202730097U (en) Novel flavor production line
CN202015506U (en) Falling film evaporator
CN205027140U (en) Modified industrial stoves discharge flue
CN203949162U (en) Rotary Kiln oxygen-enriched burning device
CN206113686U (en) Air lock gas outlet gas -liquid separation structure for battery
CN205995229U (en) A kind of flue gas separating purifying device
CN201969368U (en) Vacuum desolventizer
CN204214283U (en) Gas melting furnace flue cooling tower

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150218

Termination date: 20170926

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