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遼寧東大粉體工程技術有限公司

主營產品: 電石渣干燥機,菱鎂礦干燥機,菱鎂礦煅燒爐,電石渣煅燒爐,碳酸鈣煅燒爐,硫石膏煅燒設備,硫石膏干燥設備,碳酸鈣干燥設備

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公司信息

人:
張繼宇
話:
86-024-23996440
機:
13904004886
真:
86-024-23996440
址:
沈陽市渾南新區天賜街5-1號 國貿中心A座24
編:
110015
化:
www.lnddft-1.com
址:
www.lnddft.com
鋪:
http://www.iqjiance.com/st1081/
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[供應](斯德)鉬精礦焙燒工藝
(斯德)鉬精礦焙燒工藝
產地:
沈陽市沈河區彩塔街19號
更新時間:
2025-03-07 21:00:07
有效期:
2025年3月7日--2025年9月7日
已獲點擊:
457
【簡單介紹】
【詳細說明】

經過浮選得到的【鉬精礦】及【焙燒】前的鉬精礦都存在著【干燥問題】。特別是經過浮選的鉬精礦,雖然經過了一定的過濾、壓濾,其水分含量仍然很高。為便于運輸及下道工序的加工,必須經過干燥,使其達到規定的含水率。鉬精礦的干燥方法及使用的設備種類很多,干燥效果各不一樣。

目前,江西銅業公司德興銅礦采用了一套由【遼寧東大粉體工程技術有限公司】開發研制的一套【斯德干燥機】,對鉬精礦進行干燥,取得了較好的干燥效果,該套裝置在國內為*應用,現在已充分顯示出了它的*性能,產量大,能耗低,含水率可調。德興銅礦所生產的鉬精礦是銅礦副產鉬精礦,生產過程工藝條件具有一定的特殊性。所選的鉬精礦內含有較多的Na、Ca等雜質成份。這些有害成份,對高溫干燥過程亦有一定的影響。因此,在采用斯德干燥過程中充分注意到了這一點。利用間接換熱熱風爐所得到的潔凈熱空氣去干燥鉬精礦,避免增加干燥后鉬精礦的含雜量。控制熱風溫度、流量、流速,使進入斯德干燥機內的熱空氣與鉬精礦充分攪拌、混合。

鉬精礦在斯德干燥機內呈高度分散狀態存在于熱空氣流體中,由于鉬精礦與熱空氣能夠充分的混合,且懸浮于斯德干燥機內,因此干燥過程快而充分。該混合流體經除塵器,鉬精礦被收集,含濕廢氣經風機排空,全過程可控。

現應用企業名錄:欒川鉬業集團

                        上海云翔礦業有限公司(上海云翔泰國公司)

                        朝陽金達鉬業集團

                        江西銅業德興礦

                         近20家國內外企業。

 

Preface

At the present time most of the corporations use both reflect kilnout heating rolling kiln in China. And most of corporations abroad use multi chambers kilns.

As the development of molybdenum products market, the performance of the calcinerend gas controlling effect the corporation’ benefit.

The inner heating equipments designedmanufactured by our Co. used in molybdenum dryingcalciningthe end gas controlling is more advanced than traditional ones in technology.

Process schemethe system configuration

 The system consists of the main parts of moly drying, inner heating rolling kiln system, collecting system,mixing air system of direct heating furnace of burning coal.

 

 The processes are as follows:

Put the moly concentrate powder into the dryer to dryto average particle,then the dried powder be fed to the bunker by conveyor, then to the kiln. Being the source of heating air the direct heating furnace supports hot air to rolling kiln to calcining the molybdenum.          

The gas of sulfur dioxide generated during the production is treated by temperature adjuster, cyclone collector, bag collector,static dust catcher. The air treated is let out. The treatment method of sulfur dioxide can be sodium sulfiimestone. The first one cost higherthe other one is simplemuch cheaper.

The main technology is in:

1. Using direct inner heating rolling kiln to calcine can make the life of the equipment much longerheighten the thermal efficiency much.

 

2. The system equipped with dryer can reduce the acid materials out. As the materials being average therefore the calcining is full.

         

3. The system uses two collecting system the rate of collection is high.

 

4. The system is in the tiny negative pressure operation there is no dust out. The rate of collection is heightened.

 

 Data of the system technologyperformance

 

The detail is as follows:

 

1. Capacity : One system produces moly oxide 78 ton / h.

 

2. sulfur content in moly oxide is 0.07%

 

3. One ton moly oxide production cost standard coal about 350 KG.

 

4. One ton moly oxide production cost electricity 280kwh.

 

5. Rate of collection of the dust 99.5%

 

6. The energy for the system is about 120 kw.

 

 

The details the system configuration

 

The details is as follows:

 

                               List of equipment

 

name of the system

No.

name of the equipment

quantity

remark

drying system

1

sksz45 dryer

1 set

multi-collector

2

feeder

1 set

adjusting speed

3

hot air furnace

1 set

 

4

cyclone separator

1 set

dump valve

5

bag collector

1 set

dump valve

6

air blower

1 set

standard

7

high pressure draft fan

1 set

standard

8

draft fan

1 set

standard

9

pipelines

1 set

temperaturepressure test

10

control desk

1 set

temperature meterspeed meter

source of heat system

1

hot air furnace

1 set

 

2

room of mixing air

1 set

 

3

auto coal feeder

1 set

 

4

slag remover

1 set

 

5

machine fire grate

1 set

 

6

combustion-supporting blower

1 set

 

calcining systemcollecting system

1

body of the rolling kiln

1 set

 

 

2

kiln head

1 set

 

 

3

kiln tail

1 set

 

 

4

conveyor bunker

1 set

 

 

5

discharging machine

1 set

 

 

6

cyclone separator

1 set

 

 

7

bag collector

1 set

 

 

8

blower

1 set

 

 

9

butterfly valve

1 set

 

 

10

electric butterfly valve

1 set

 

 

11

heat exchanger

1 set

 

 

12

pipeline system

1 set

 

 

13

controlling system

1 set

 

 

14

pulse pump

1 set

 

price

RMB1,765,000.00

remarks

1. designing fee RMB 100,000.00    2. training fee RMB 26,400.00

total: RMB126,400.00

 

Design time 15 work days          

Manufacture time 80 100 days

1. Design feetraining fee RMB 126,400.00 should prepay in one time in one week.

Seller supply:

1 seller sets the engineers to the plant to direct installation, train operator, adjusttest equipments

2 seller supplies groundwork draws, process draws, pipeline connecting drawscontrolling draws.

3directing installing time are 30 workdays, adjusting times are 7 workdays 

2. Buyer supplies the traveling expenses, foodaccommodation.

3. Buyer supplies cablewire from controlling board to the machines.

4. touch-up painting is led by buyer.

5. The materials that the part touches the materials being dried are made from carbon steel.  

 The materials that the part touches the materials being calcining are made from refractories. The conveyor is made from carbon steel.

6. Buyer supply the pipes for draft fan

7. Some parts of equipment should be welded at the locale, buyer pays for it.

8. Platform, bracket, guardrail should be made at the locale, buyer pay for it ,seller supplies the draws of them. 

 

Remarks

 

Every production line is made a single system according to the buyer. The workshop would be designed for two production lines. The area for part of calcining is 24×50×10 M2, for end gas treading is 24×50×10 M2.

The processes will be adjusted if need.

 

 

 

 

 

 

 

 

 

 

 

 



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