Abstract:
The present invention relates to a “method of recycling wasted printed-circuit-board”, which takes advantage of the characteristics of the PCB so as to dispose different recycling material in stage manner, so that different metals remaining on said PCB are sorted out step by step; Thereby, the bromide and the fiberglass of importance in the resins are collected and converted into variety of industrial materials as resource for recycling use in order to prevent said wasted PCB from spoiling the natural environment after recycling use.

Description:
FIELD OF THE PRESENT INVENTION 
       [0001]    The present invention relates to the method of recycling wasted printed-circuit-board, particularly for the method and equipment thereof in collecting the different metals remaining on the recyclable wasted PCB being converted into recycling industrial materials under the standard of avoiding second pollution. 
       BACKGROUND OF THE INVENTION 
       [0002]    As everyone knows, the PCB has been largely used in variety of electric products; Worryingly, the heavy metals in the wasted PCBs such as tin, lead and copper etc. can easily cause second social effects of pollution if those wasted PCBs did not collected for recycling or disposed unsuitably when they are discarded as junk; Especially, the brominated epoxy resins of halide in said wasted PCBs are much easier to spoil natural environment; that is why all the environmental protection experts of every country in the world without exception strive for advocating in reducing the utility rate of using halide materials. 
         [0003]    Therefore, every country in the world takes the wasted PCBs into noxious entrepreneurial junk under the environmental protection control; Presently, the relating industries already developed some methods to collect and recycle the metal materials and the fiberglass of intermediate material in the wasted PCB, they are comminuting method [for example: the patent numbers of 247281 and 363904 in the patent publication of TAIWAN R.O.C.], direct incinerating method, heating decomposition method, chemical dissolving method and melted inorganic salt method; However, while recycling disposal of the wasted PCB, some drawbacks still exist in these methods aforesaid as bellow. 
         [0004]    1. Comminuting Method: 
         [0005]    First pulverize the wasted PCBs into powder, then sort said powder into two categories of more metallic powder and less metallic powder; Regardless of what kind of powder aforesaid, the ingredients contain mixture of brominated epoxy resins and fiberglass in addition of the metal so that causing not only impurity effect but also certain difficulty in recycling disposal; Especially, both of the recycling value of said brominated epoxy resins and fiberglass after collecting are neglected. 
         [0006]    2. Direct Incinerating Method: 
         [0007]    Directly incinerate and melt the wasted PCBs into mixture of fiberglass and metal, then extract the essential metals after cooling; The process not only consumes much energy but also creates environmental pollution issue owing to the toxic hydrogen bromide [BrH] byproduct; Besides, the collected materials, which are low-grade mixture of metal, must re-smelt to purify for recycling use so that the value of direct utilization is very low. 
         [0008]    3. Heating Decomposition Method: 
         [0009]    A tremendous amount toxic hydrogen bromide [BrH] gas is produced during heating decomposition process so that seriously jeopardizing natural environment; Excepting the metal being recyclable by sorting, the rest materials such as brominated epoxy resins and fiberglass are not recyclable with potentiality of spoiling environment. 
         [0010]    4. Chemical Dissolving Method: 
         [0011]    The metal in the middle layers of the wasted PCBs can not be completely dissolved during dissolving process so that the brominated epoxy resins being mixed up with heavy metals after dissolving process; Thus, the issue of environmental protection still exists. 
         [0012]    5. Melted Inorganic Salt Method: 
         [0013]    Collect and recycle metals and fiberglass by putting the wasted PCBs into melted inorganic salt, which having drawbacks as below: 
         [0014]    a. Upon processing temperature over 400° C., the tin, lead and copper in said wasted PCBs will mix into alloy such that becoming low-grade metal mixture, which not only incurring extra cost expense but also wasting time and effort for refinement. 
         [0015]    b. The wasted PCBs will float on the melted inorganic salt as the specific weight of the melted inorganic salt is greater than that of the wasted PCBs; Thereby, the agitating separation process is difficult to directly operate. 
         [0016]    c. The agitating shattering process will fail as the wasted PCBs softening with flexibility after the dissolution of the melted inorganic salt. 
         [0017]    d. The finished PCBs are interconnected by electroplating joint with soldering point being bigger than through-hole such that fiberglass of PCBs being tightly bonded; Thereby, the effect in separating process of fiberglass is relative low due to difficulty. 
         [0018]    e. The fiberglass will be ruined as the wasted PCBs being put in the melted inorganic salt over a long period of time; The collecting of said fiberglass is difficult as operating time in the mix-agitating process and the re-extracting process is uncontrollable and inconsistent; 
         [0019]    Meanwhile, the recycling feasibility of shattered fiberglass is relatively reduced. 
         [0020]    Accordingly, all the conventional methods aforesaid in disposing wasted PCB are not the ideal perfect disposal method. Therefore, the present invention originates a stepwise way to collect and recycle different materials by different method and step at each stage in accordance with the characteristics of the PCB so as to achieve in creating the best recycling value in consequence of perfect collecting and recycling. 
       SUMMARY OF THE INVENTION 
       [0021]    The present invention originates a method of recycling wasted printed-circuit-board, whose prime object is to stepwise collect and recycle different materials in the wasted PCB in manner from outer towards inner way in accordance with the structural characteristics of the PCB; Additionally, a suitable recycling procedure is designed in accordance with recycling value such that recycling material obtaining highest recycling value; Thereby, an integrated recycling system is worked out for the everlasting plan in PCB industry. 
         [0022]    In other words, the present invention takes advantage of the characteristics of the PCB so as to dispose different recycling material in stage manner, so that different metals remaining on said PCB are sorted out step by step; Thereby, the bromide and the fiberglass of importance in the resins are collected and converted into variety of industrial materials as resource for recycling in order to prevent said wasted PCB from spoiling the natural environment after recycling. 
     
    
     
       BRIEF DESCRIPTION OF THE DRAWINGS 
         [0023]      FIG. 1  is the disposal flow chart of the present invention. 
           [0024]      FIG. 2  is the illustrative view of the wasted PCB after chemical reaction in the melted sodium nitrate of the present invention. 
           [0025]      FIG. 3  is the illustrative view of the recycling equipment thereof to operate in coordination with the present invention. 
       
    
    
     DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS 
       [0026]    As shown in the figures of number  1  and  2 , the present invention is a method of recycling wasted printed-circuit-board with disposal steps comprising: 
         [0027]    a. Remove all electronic components on all wasted PCBs  10  by heating them on their soldering points such that becoming wasted PCBs without any electronic component then collectively sort and dispose them for recycling use. 
         [0028]    Heat all such wasted PCBs without any electronic component over to 200° C. to melt soldering tin on their surface layer so as to remove and collect the tin-contained-compounds, whose melting point being 200° C.; then directly collect them by vacuum tin-sucking method for recycling use. 
         [0029]    c. Soak said wasted PCBs at step b in de-tin solution of market finished product to dissolve the tin-contained-compounds in the inner layers to separate it from copper; then directly collect all of tin-contained-compounds by said de-tin solution for recycling use. 
         [0030]    d. Apply strong acid solution on said wasted PCBs at step c to dissolve the spot-welding copper and electroplating copper in the through-hole out such that becoming wasted PCBs without any copper foil; Wherein, used strong acid solution will become acid solution containing copper ion [Cu ++ ] being able to serve as etching solution, and some copper pathways in the inner layers still mix up with fiberglass owing to no contacting with said strong acid. 
         [0031]    e. Soak said wasted PCBs at step d in melted sodium nitrate  20  to proceed heating decomposition chemical reaction to separate brominated epoxy resins from fiberglass so as to produce sodium bromide  11 , carbonized fiberglass  12 , copper foil  13 , organic gas  14  and nitrogenous oxides  15 ; 
         [0032]    Wherein, said sodium bromide  11  can be directly discharged and collected due to harmless to environmental safe, and said organic gas  14  and nitrogenous oxides  15  will become stable nontoxic gas to be discharged out after complete combustion. 
         [0033]    f. Separate carbonized fiberglass  12  and copper foil  13  by applying water rinsing method on their mixture formed above; then directly collect said carbonized fiberglass and copper foil for recycling. 
         [0034]    Wherein, the strong acid solution used in step d aforesaid can be the diluted nitric acid, either hydrochloric or sulfuric acid mixing with a little nitric acid to sprinkle on said wasted PCBs under oxygen environment. 
         [0035]    Furthermore, the detail of step d aforesaid is shown in the FIG.  2 ., employ melted sodium nitrate  20  to directly decompose brominated epoxy resins such that sodium ion [Na + ] and bromine ion [Br − ] immediately combining into stable sodium bromide  11 ; Thus, air pollution and environment pollution can be prevented by discharging said bromide out with gas. After heating decomposition, said epoxy resins will becomes organic gas  14  and black carbon, which adhering to the fiberglass  12 . Additionally, the sodium nitrate  20  becomes a nitrate radical ion [NO 3   − ] due to losing its sodium ion [Na + ]; both of said organic gas  14  and nitrate radical ion [NO 3   − ] will become stable gas after oxygenated combustion; Next, the toxic material contained can be easily removed via operating in coordination with water rinsing dirt-removal device; Thus, not only the bromine element can be collected for recycling use but also the carbonizing of the fiberglass can be enhanced as said fiberglass must via carbonizing reinforcement and increasing surface area to have application convenience for being favorable in recycling use. 
         [0036]    Moreover, after water rinsing method in the step f aforesaid, in the mixture of said carbonized fiberglass  12  and copper foil  13 , said carbonized fiberglass  12  will float upwards on the water solution while said copper foil  13  will precipitate downwards due to different specific weight comparing to that of water solution respectively; Thereby, the collecting and recycling process of carbonized fiberglass  12  and copper foil  13  becomes easier. 
         [0037]    Thus, via all the process steps aforesaid applying on said wasted PCBs  10 , all the constituents of the soldering tin, copper, brominated epoxy resins and fiberglass can be easily separated respectively; 
         [0038]    Hence, we can adequately work out solutions for both of pollution preventing and product recycling issues through above separating process. Comparing to all conventional process methods of prior art mentioned above, the process method of the present invention has following advantages: 
         [0039]    1. Being a nondestructive manner, the process of the present invention has good economical effect as not incurring any recycling cost increase due to destroying material chemical structure. 
         [0040]    2. Each process step of the present invention has recycling value effect in easy feasibility and resulting in not only substantially reducing the equipment investing cost but also being simple and convenient in operation. 
         [0041]    3. The entire recycling process of the present invention can ensure in avoiding and preventing second pollution with reasons as bellow:
       (1) The nitric acid de-tin solution and hydrochloric acid de-tin solution used in the tin dissolving process is existing market finished product with mature process effect.   (2) The strong acid used in the copper dissolving process is same as the etching solution used in the conventional PCB manufacturing process so that it can be directly collected to serve as etching solution for recycling use.   (3) Employ strong oxidizing agent to directly decompose brominated epoxy resins such that sodium ion [Na + ] and bromine ion [Br − ] immediately combining into stable bromide and resulting in preventing second pollution.   (4) The black carbon, attaching on the fiberglass with intact large surface area after heating decomposition, not only make itself increase in the recycling feasibility and process easiness but also make said fiberglass save heating energy in carbonization for being directly collected as recycling material.   (5) The fiberglass can be easily collected and recycled via simple water rinsing method.   (6) The copper foil can be easily collected and recycled via simple water rinsing method too.   (7) Separating the sodium bromide and sodium nitrate is not difficult owing to their difference in physical properties, namely the melting point is 300° C. and specific weight is 2.261 for said sodium nitrate while the melting point is 757.7° C. and specific weight is 3.203 for said sodium bromide.   (8) All the variety of recycling materials can create good recycling value without any waste in the process.       
 
         [0050]    Regarding the method for undertaking the heating decomposition in providing said wasted PCBs  10  and sodium nitrate  20 , the equipment thereof in recycling wasted printed-circuit-board in the present invention comprises a furnace  30  and a heater  40 ; Wherein, said furnace  30  comprises a feeding inlet  31 , a discharge valve of sodium bromide  32 , an gas complete-combustion apparatus  50  and a production outlet  34 ; 
         [0051]    For said feeding inlet  31  with double doors design of exterior door and interior door has working safety in consequence of preventing internal gas from leaking out by means of their interlocking protection of said double doors; Whose operation way is that first put the wasted PCBs  10 , which containing brominated epoxy resins and fiberglass, together with the sodium nitrate  20  inside while exterior door being open and interior door being closed; next guide said wasted PCBs  10  and sodium nitrate  20  into said furnace  30  while exterior door being closed and interior door being open; then close the interior door after all feeding stuff getting into said furnace  30  such that double doors in closed status. 
         [0052]    Said discharge valve of sodium bromide  32  is to discharge the mixing liquid of said sodium nitrate  20  and sodium bromide  11  out of said furnace  30  after heating decomposition chemical reaction, wherein said sodium bromide  11  being at the undermost of said furnace  30  due to heavier specific weight than that of said sodium nitrate  20 ; 
         [0053]    Said outlet tractor of fiberglass  33  is to draw the carbonized fiberglass and copper foil to said production outlet  34  after heating decomposition chemical reaction, so that subsequently undertaking water rinsing outside of said furnace  30  via said production outlet  34  so as to obtain pure carbonized fiberglass  12  and pure copper foil; 
         [0054]    Said heater  40  is to heat said sodium nitrate  20  up to between 350° C. and 500° C. such that said sodium nitrate  20  becoming melted state. 
         [0055]    Thus, via all equipment aforesaid, heating decomposition chemical reaction of said wasted PCBs  10  and sodium nitrate  20  happens in said furnace  30  and the sodium bromide  11 , carbonized fiberglass  12 , copper foil  13 , organic gas  14  and nitrogenous oxides  15  are obtained respectively; Wherein, said sodium bromide  11 , fiberglass  12  and copper foil  13  are drawn out of the furnace  30  by said outlet tractor of fiberglass  33  such that removing said sodium bromide  11  and sodium nitrate  20  by water rinsing to obtain carbonized fiberglass  12  and copper foil  13  as industrial materials for recycling use; 
         [0056]    And, said organic gas  14  and nitrogenous oxides  15  will be converted into stable gas  141  after complete combustion in the gas complete-combustion apparatus  50  and water rinsing in the water rinsing dirt-removal device. As shown in the  FIG. 3 , said gas complete-combustion apparatus  50  mainly comprises a circulating reactor  51 , an oxygenated combustion-supporting reactor  52 , an air reaction buffing retainer  53 , a second heating burner  54 , a blower  55 , an air heat-exchanger  56 , a furnace cooler  57 , an air dirt-removal cooler  58  and a pressure equilibrator  59 ; 
         [0057]    Wherein, said circulating reactor  51 , which being built in the furnace  30 , is to control the reaction time of said wasted PCBs  10  and melted sodium nitrate  20  by transmission speed of connected motor so as to ensure the quality of the fiberglass  12  not being spoiled; 
         [0058]    Said oxygenated combustion-supporting reactor  52 , which being put above said circulating reactor  51  in the furnace  30 , is to supply compressed oxygen so as to enhance the complete combustion of said organic gas  14 ; 
         [0059]    Said air reaction buffing retainer  53 , which being constructed above said oxygenated combustion-supporting reactor  52  in the furnace  30 , is to stabilize and expedite the gas inside in chemical combination with oxygen of hot air; 
         [0060]    Said second heating burner  54 , which being put above said air reaction buffing retainer  53 , is to increase the reaction temperature in the furnace  30  so as to ensure said organic gas  14  being combusted more completely during second combustion as well as to let air dirt-removal cooler  58  cool them down to become stable gas  141  meanwhile; 
         [0061]    Said blower  55 , which being disposed above the furnace  30 , is to inhale a great quantity of external air into said furnace  30  such that said organic gas  14  and nitrogenous oxides  15  complete combusting quickly so as to eliminate the incomplete combustion phenomena of those gas; 
         [0062]    Said air heat-exchanger  56 , which being built above said second heating burner  54  over the furnace  30 , is to warm and activate the intake cool air by temperature of said furnace  30  so as to have multiple enhancing effects as not only increasing the activity of oxygen for combustion but also reducing the consumption of fuel material as well as accelerating the reaction speed; 
         [0063]    Said furnace cooler  57 , which being put on the furnace  30 , is to exchange heat between the cooling water and the temperature of said furnace  30  under principle of heat exchange so as to cool down the temperature of said furnace  30 ; 
         [0064]    Said air dirt-removal cooler  58  is to remove the dirty material via dust-filtering and adsorption for the gas after combustion, which being then discharged outside after dirt-removal handling to prevent second pollution; 
         [0065]    Said pressure equilibrator  59  is to detect and measure the negative pressure in the furnace  30  by pressure transducer, then to adjust the speed of windmill via regulation of the frequency converter by means of pressure controller so as to further equilibrate the pressure in said furnace  30  such that said organic gas  14  being processed in single adequate direction; 
         [0066]    Therefore, concluding the exemplary embodiment aforesaid, it is justified that such gas complete-combustion apparatus  50  can really convert the organic gas  14  and nitrogenous oxides  15  into nontoxic stable gas  141  after heat decomposition; Thus, whole process absolutely conforms to every regulations of the environment protection as no harmful material being discharged out.