Abstract process experimental period of nearly two years of production and that the fluoroboric acid system to 2,4-- dichlorobenzaldehyde as Additive Sn-Pb alloy plating mirror bright, process stability.
I products are more silver plated member, but after a period of time is placed silver black, solderability and resistivity will be greatly affected. After DJB-823 is applied, its appearance is affected, and it is necessary to have conductivity under a certain pressure. Therefore, it is imperative to develop a silver-based material.
At that time, many reports that Sn-Ce alloy was a better silver substitute material, we started this process test, but the effect was not satisfactory. So we developed the bright Sn-Pb process, first around the purchase of commercial additives test, but the effect is not ideal, mainly because the coating is not bright, the solution is unstable, so we checked the data and in-depth test, finally found a comparison Good process specifications, after two years of trial production, the performance is quite stable. There are no additives in almost two years, but always keep the high current plating and plating mirror bright. Today I will introduce the work of these years to everyone, I hope everyone can benefit from it. .
1 Process specification
1.1 Process recipe Sn 2+ 18-25g/l
Pb 2+ 8-11g/l
HBF 4 (free) 250-300g/l
H 3 BO 3 : 10-30g/l
OP21 10-30g/l
2.4-dichlorobenzaldehyde lg/l
O-toluidine 6-10ml/l
HCHO 5-15g/l
Dk 5-15A/dm 2
Cathode movement 40-60 times / min
Tem room temperature 1. 2 process
Pretreatment - copper cyanide base - cleaning - plating Sn - Pb - cleaning - passivation - cleaning - drying - inspection [next]
1.3 Precautions 1.3.1 Additives Add 2,4-dichlorobenzaldehyde to o-toluidine for a period of time, then add OP21, HCHO can be added to the bath separately.
1.3.2 The workpiece should not be placed too dense to prevent local fogging.
1.3.3 If the bath has not been used for a long time, test the current density range with HULL before plating.
1.3.4 The coating is bright, so it is supplemented by high-speed cathode movement.
1.3.5 Suitable for iron and copper alloy substrates.
1.3.6 Unqualified plating removal is carried out in the usual way.
2 plating quality inspection
2.1 Appearance The coating is blue with a mirror finish.
2.2 Bonding force according to SJ1282—73 qualified 2.3 third-order performance
Execution according to GJB367, 2-87, wet heat and salt spray test, qualified 2.4 welding performance
Better than silver plating, good fluidity.
3, Conclusion <br> The process has been put into production in 1995, the effect is very good, the coating mirror is bright, and the efficiency is very high, for high-current electroplating, generally plating for 5-10 minutes, from the solution to the present, has not been adjusted once and supplemented The additive proves that the performance of the plating solution is extremely stable. The disadvantage is that the plating solution is a fluoroboric acid system, which has certain requirements for environmental protection, but the process is much better than the many additives at home and abroad in terms of production, which is us. Do a lot of conclusions from comparative experiments.
References 1, Zeng Hualiang, etc., "Electroplating Process Manual" Machinery Industry Press 1993
2, (United States) Frederick "Modern Electroplating" Machinery Industry Press 1982
3. Chen Lizhen, Tsinghua University Science Report, 1979

Batch Waste Tyre Pyrolysis Plant

Pyrolysis Plant is used for recycling waste tire, waste plastic, waste rubber to fuel oil. According to the actual situation in every country and district, we developed different models of Batch Pyrolysis Plants for waste tires, rubber and plastic with daily capacity 5 -10 tons.

Batch Waste Tyre Pyrolysis Plant

Flowchat of Batch Waste Tyre Pyrolysis Plant

Batch Waste Tyre Pyrolysis Plant 

Advantages of Batch Waste Tyre Pyrolysis Plant

 

1. Full open door design: Speedy loading in and steel pulling out; Easily cooling down after one batch finished, saving time; No leaking with special high temperature flexible graphite packing.

2.  Unique Craft Condensers: High condensing efficiency with more oil output. Good quality oil, longer lifetime, and easy to clean.

3.  National Patent Unique Smoke Scrubbers: More efficient removal of the acid gas and dust of the smoke by neutralization, purification and absorption, environmental friendly without pollution.

4. National Patent Carbon Black Discharging System: Speedy fully enclosed Auto-discharging under high temperature, avoiding carbon black pollution, saving time.

5.  Automatic Submerged welding technology, ultrasonic nondestructive testing, both manual and the automatic safety devices.

6. Sync Gas Recycling System: Fully burned after recycling and utilization, saving fuel and preventing pollution.

7. Direct Heating System: Enlarging heating square to lengthen the lifespan of the reactor and easy to control the temperature.

8. National Patent, unique heat insulation shell; high efficiency temperature keeping, excellent energy-saving effect.

 

Technical Parameter of Batch Waste Tyre Pyrolysis Plant

NO.

ITEM

PROJECT

1

Equipment Model

XY-7

XY-8

2

Door Model

Full Open Door

Full Open Door

3

Suitable Raw Materials

Rubber/Plastic Products

Rubber/Plastic Products

4

Structure

Horizontal Type Revolves

Horizontal Type Revolves

5

Reactor Size

Φ2200*6000mm  Î¦2600*6600mm

Φ2200*6000mm  Î¦2600*6600mm

6

Capacity for One Batch

5-6Mt; 8-10Mt

5-6Mt; 8-10Mt

7

Oil Yield of Tires

40%-45%

40%-45%

8

Work Pressure

Normal Pressure

Normal Pressure

9

Reactor Rotation Speed

0.4R/M

0.4R/M

10

Fuels Choice

Coal, Wood

Coal, Wood, Gas, Oil

11

Power

18KW/H

18-25KW/H

12

Cooling Method

Water Cycling

Water Cycling

13

Type of Drive

External Annular Gear

External Annular Gear

14

Heating Method

Direct

Direct

15

Type of Installation

With Foundation

With Foundation/Integrated Base

16

Noise dB(A)

≦85

≦85

17

Operation Mode

Intermittent Operation

Intermittent Operation

18

Total Weight(MT)

25-40

25-40

19

Installation Space Required

30m*10m

30m*10m

20

Manpower

3~4/batch

3~4/batch

21

  Shipment

Ф2200×6000=1*40HC+1*40FR

Ф2600×6600=2*40HC+1*40FR

Ф2200×6000=1*40HC+1*40FR

Ф2600×6600=2*40HC+1*40FR

 

Batch Waste Tyre Pyrolysis Plant

Batch Waste Tyre Pyrolysis Plant,Waste Tyre Pyrolysis Plant,Rubber Pyrolysis Recycling Plant

Shangqiu Jinpeng Industrial Co., Ltd. , https://www.recyclings.nl