CN1520943A - Method and apparatus for processing waste containing bromination epoxy resin and glass fiber - Google Patents
Method and apparatus for processing waste containing bromination epoxy resin and glass fiber Download PDFInfo
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- CN1520943A CN1520943A CNA031023746A CN03102374A CN1520943A CN 1520943 A CN1520943 A CN 1520943A CN A031023746 A CNA031023746 A CN A031023746A CN 03102374 A CN03102374 A CN 03102374A CN 1520943 A CN1520943 A CN 1520943A
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- heater
- epoxy resin
- glass fibre
- brominated epoxy
- waste products
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Abstract
The present invention is method and apparatus for treating waste containing epoxy resin bromide and glass fiber. Waste containing epoxy resin bromide and glass fiber is thrown into molten inorganic salt, so that the waste reacts with inorganic salt and is decomposed thermally and epoxy resin bromide and glass fiber are separated automatically to obtain bromate, glass fiber and organic gas. The organic gas is burnt completely in the burning device to convert into water vapor and CO2 harmless to environment. The apparatus includes one furnace with double-layer door material feeding port, valve for exhausting inorganic salt and glass fiber drawing discharger; one heater; and one gas completely burning device. The present invention has simple apparatus, low waste processing cost and high processing effect and is favorable to environment protection.
Description
＜one〉technical field
The present invention a kind of processing method and device thereof to the waste products that contains brominated epoxy resin and glass fibre, mean that a kind of waste products that will contain brominated epoxy resin and glass fibre adds in the inorganic salts of fusion, comes hot tearing to solve the method and the device of the raw materials of industry such as Bromide class and glass fibre.
＜two〉background technology
Epoxy resin is a kind of filler of fairly good usefulness, but its shortcoming is inflammable, so in order to improve its flame resistance, at present all be this epoxy resin to be handled through bromination obtain the high brominated epoxy resin of flame resistance (DGETBA), and because this brominated epoxy resin also has the characteristics such as adhesive force of splendid insulating properties and enhancing and metal, so present industrial circle often is to utilize this brominated epoxy resin as solid, it is bonding to make the engineering plastic plate except being used for glass fibre, also be used in large quantities on the various electric products simultaneously, for example as the insulating materials on electric, circuit board, or other special spare part etc.; Only, this contains the engineering plastic plate or the other products of brominated epoxy resin, in case become waste products, the glass fibre that recyclable recirculation is used in its structure, and can't recycle in the mode of incinerating, and, this waste products is molten condition time receiving back and forth if being heated to this glass fibre, the high-temperature service that then must setting can be heated to more than thousands of degree ℃ can be reached, do not meet economic benefit, in addition if reclaim glass fibre in the waste products in the mode of thermal cracking, this brominated epoxy resin can produce the hydrogen bromide (BrH) of serious environment pollution again in its process, so in recent years in the waste products for engineering plastic plate that contains brominated epoxy resin or other products, it is infeasible reclaiming glass fibre at all, it only can let alone to stack wantonly, and this not only causes the waste of resource, and the tough structure that is difficult to decompose of this waste products killer that destroys environment especially.
The present invention's main purpose is to utilize the molten salt can be directly and the characteristic of bromine reaction, this is contained the inorganic salts of putting into fusion in the waste products of brominated epoxy resin, can produce stable harmless bromination salt (as sodium bromide) after making its reaction, and can work as the organic gas of fuel as energy recovery, cleavable reclaims pure glass fibre again simultaneously, and uses for recycling as the raw material of industry.
The present invention's another purpose, be hot tearing to solve highly purified glass fibre with the molten salt class of 300 ℃ to 500 ℃ of temperature, do not need to use and have the firing equipment that is heated to more than thousands of degree ℃, make whole recovery handle the more simple and easy and reduction processing cost of process of glass fibre, and meet the economic benefit of recovery.
Another object of the present invention, but be that a completing combustion apparatus is being provided, must when this molten salt thermal cracking brominated epoxy resin, after the organic gas completing combustion that is produced, change into the steam and the carbon dioxide of environmental sound.
＜three〉summary of the invention
A kind of processing method of the present invention to the waste products that contains brominated epoxy resin and glass fibre, it is that a waste products that contains brominated epoxy resin and glass fibre is fed in the inorganic salts of fusion, make the inorganic salts of this fusion can be directly and the bromine in the brominated epoxy resin produce reaction, and to this waste products generation thermal cracking, separate thereby make this brominated epoxy resin can produce voluntarily, and obtain bromination salt, pure glass fibre and organic gas respectively with glass fibre.Wherein, this bromination salt is environmentally safe harmless and can directly discharge, this pure glass fibre then can use for recycling as the raw material of industry, and this organic gas system uses a completing combustion apparatus, will change into the steam and the carbon dioxide of environmental sound after its completing combustion; Inorganic salts among the present invention are potassium nitrate or ammonium nitrate or nitrite natrium or nitric acid is received or above-mentioned two or more mixture; And this organic gas system comprises: hydrogen (H
2), water (H
2O), carbon monoxide (CO), carbon dioxide (CO
2), methane (CH
4), ethane (C
2H
6), the rare (C of second
2H
4), acetylene (C
2H
2), methyl alcohol (CH
3OH), ethanol (C
2H
5OH), C
3(propane, third rare, acetone, propyl alcohol etc.), C
4(butane, fourth are rare, butanone, butanols etc.), C
5, C
6Or the like.
A kind for the treatment of apparatus of the present invention to the waste products that contains brominated epoxy resin and glass fibre, it is to contain the waste products of brominated epoxy resin and glass fibre and the device of the capable thermal cracking of molten salt for this, is to comprise a body of heater and a heater; Have a feeding mouth on this body of heater, inorganic salts draw off valve, a glass fibre discharging tractor and a discharging opening; Wherein, this feeding mouth system adopts the two door design of external door and inside door, and it is that this waste products and inorganic salts are put into to external door in advance, in opening again goalkeeper its lead put into this body of heater after, can be by the interlock protection of this inside and outside door, it has the security that prevents internal gas outflow and work; These inorganic salts draw off valve then behind heat scission reaction, and the inorganic salts of fusion in the stove are discharged into outside this body of heater; This glass fibre discharging tractor then is drawn to glass fibre pure behind the heat scission reaction this discharging opening place, sends this body of heater by this discharging opening again and cleans outward, can obtain pure glass fibre; This heater is that these inorganic salts are heated between 300 ℃ to 500 ℃, makes these inorganic salts be molten condition person.
Wherein, this treating apparatus comprises that more one is used for the gas smoke consumer of this organic gas of completing combustion, and it has a recirculation reactor, an oxygen enriching burning-aid reactor, air reaction buffering stop device, a post bake burner, an air blast, an air heat exchanger, a body of heater cooler, an air scrubbing cooler and a pressurizer; Wherein, this recirculation reactor system is arranged in this body of heater, and it is the reaction time of controlling the inorganic salts of this waste products and fusion with the transmission speed of motor, is not destroyed with the quality of guaranteeing glass fibre; This oxygen enriching burning-aid reactor system is arranged in this body of heater, and it is the oxygen that compression is provided, and increases the completing combustion of this organic gas; This air reaction buffering stops device system and is arranged in this body of heater, and it has the effect that the interior gas of stable body of heater reaches fast and the oxygen in the hot-air combines; This post bake burner system is arranged on this body of heater, is used for improving the reaction temperature in the body of heater, makes this organic gas when carrying out second-time burning, can guarantee that burning is more complete, and produce steam and carbon dioxide simultaneously; This air blast system is arranged on the body of heater, and its air that external world is a large amount of is fed through in the body of heater, and this organic gas can quick and completely be burnt, and gets rid of phenomenons such as gas combustion is incomplete fully and produces; This air heat exchanger system is arranged on the body of heater, and it is to heat up after the activation entering cold air in the body of heater with furnace temperature in advance, makes the oxygen activity in the body of heater internal combustion stronger, and then reduces the loss of fuel and increase multinomial gains such as reaction speed; This body of heater cooler system is arranged on the body of heater, and it utilizes heat exchange principle that cooling water and furnace temperature are done heat exchange, reduces this stove body temperature; This air dirt separator is that effects such as gas permeation dedusting after the burning and absorption are disposed to the external world again, prevents the generation of secondary pollution; This pressurizer is to utilize pressure to detect the negative pressure value of measuring in this body of heater, directly control windmill gravitation with pressure controller control frequency converter again, and then reach the effect of balance body of heater internal pressure, and allow this organic gas handle simultaneously according to single direction.
The present invention a kind of processing method and device thereof to the waste products that contains brominated epoxy resin and glass fibre, its advantage is: method is simple, and technological equipment easily disposes, and the processing cost of waste products is low, and is effective, helps environmental protection.
＜four〉description of drawings
The step calcspar of Fig. 1 the present invention's method.
Fig. 2 the present invention's schematic representation of apparatus.
Number in the figure is as follows:
10 waste products, 11 glass fibres, 12 bromination salts
13 organic gas, 20 inorganic salts, 30 bodies of heater
31 feeding mouths, 32 inorganic salts draw off valve 33 glass fibre discharging tractors
34 discharging openings, 40 heaters, 50 gas smoke consumers
51 recirculation reactors, 52 oxygen enriching burning-aid reactors, 53 air reactions buffering stops device
54 post bake burners, 55 air blasts, 56 air heat exchangers
57 body of heater coolers, 58 air scrubbing coolers, 59 pressurizers
131 steam, 132 carbon dioxide
＜five〉specific embodiment
See also shown in Figure 1, a kind of processing method of the present invention to the waste products that contains brominated epoxy resin and glass fibre, it is that a waste products 10 that contains brominated epoxy resin and glass fibre is fed in the inorganic salts 20 of fusion, make the inorganic salts 20 of this fusion can be directly and the bromine in the brominated epoxy resin produce reaction, and to these waste products 10 generation thermal crackings, separate and cause this brominated epoxy resin and glass fibre to produce voluntarily, and obtain bromination salt 11, pure glass fibre 12 and organic gas 13 respectively; Wherein, this bromination salt 11 is environmentally safe harmless and can directly discharge, 12 in this pure glass fibre can use for the recirculation as the raw material of industry, this organic gas 13 is to use a completing combustion apparatus, its completing combustion is changed into the steam 131 and the carbon dioxide 132 of environmental sound, and the inorganic salts 20 among the present invention are to can be potassium nitrate or ammonium nitrate or nitrite natrium or nitric acid is received or above-mentioned two or more mixture; And this organic gas 13 is to comprise: hydrogen (H
2), water (H
2O), carbon monoxide (CO), carbon dioxide (CO
2), methane (CH
4), ethane (C
2H
6), the rare (C of second
2H
4), acetylene (C
2H
2), methyl alcohol (CH
3OH), ethanol (C
2H
5OH), C
3(propane, third rare, acetone, propyl alcohol etc.), C
4(butane, fourth are rare, butanone, butanols etc.), C
5, C
6Or the like.
See also shown in Figure 2ly, a kind for the treatment of apparatus to the waste products that contains brominated epoxy resin and glass fibre of the present invention wherein, for the device of this waste products 10 with molten salt 20 row thermal crackings, is to comprise a body of heater 30 and a heater 40; Have a feeding mouth 31 on this body of heater 30, inorganic salts draw off valve 32, a glass fibre discharging tractor 33 and a discharging opening 34; Wherein, this feeding mouth 31 is the two door design of adopting external door and inside door, it is that these waste products 10 and inorganic salts 20 that contain brominated epoxy resin and glass fibre are put into to external door in advance, in opening again goalkeeper its lead put into this body of heater 30 after, can be by the interlock protection of this inside and outside door, it has the security that prevents internal gas outflow and work; These inorganic salts draw off 32 on valve behind heat scission reaction, and the inorganic salts 20 of fusion in the stove are discharged into outside this body of heater 30; This glass fibre discharging tractor 33 is that glass fibre pure behind the heat scission reaction 12 is drawn to this discharging opening 34 places, sends this body of heater 30 outer cleanings by this discharging opening 34 again, can obtain pure glass fibre 12; This heater 40 is that these inorganic salts 20 are heated between 300 ℃ to 500 ℃, makes these inorganic salts 20 be molten condition; Can make this waste products 10 and the inorganic salts 20 of fusion in this body of heater 30, produce thermal cracking by above-mentioned device, and obtain bromination salt 11, pure glass fibre 12 and organic gas 13 respectively, wherein, this bromination salt 11 and pure glass fibre 12 are to be drawn to body of heater 30 by this glass fibre discharging tractor 33, again with bromination salt 11 on this glass fibre 12 of clear water eccysis, and obtain a pure glass fibre 12, can use for recycling as the raw material of industry; This organic gas 13 then need re-uses a gas smoke consumer 50, will change into the steam 131 and the carbon dioxide 132 of environmental sound after its completing combustion.
See also shown in Figure 2 again, a kind for the treatment of apparatus of the present invention to the waste products that contains brominated epoxy resin and glass fibre, comprise that more one is used for the gas smoke consumer 50 of this organic gas 13 of completing combustion, it has a recirculation reactor 51, an oxygen enriching burning-aid reactor 52, air reaction buffering stop device 53, a post bake burner 54, an air blast 55, an air heat exchanger 56, a body of heater cooler 57, an air scrubbing cooler 58 and a pressurizer 59; Wherein, this recirculation reactor 51 is to be arranged in this body of heater 30, and it is the reaction time of controlling the inorganic salts 20 of this waste products 10 and fusion with the transmission speed of motor, is not destroyed with the quality of guaranteeing glass fibre; This oxygen enriching burning-aid reactor 52 is to be arranged in this body of heater 30, and it is the oxygen that compression is provided, and increases the completing combustion of this organic gas 13; It is to be arranged in this body of heater 30 that this air reaction buffering stops device 53, and it has stable body of heater 30 effect that interior gas reaches fast and the oxygen in the hot-air combines; This post bake burner 54 is to be arranged on this body of heater 30, is used for improving the reaction temperature in the body of heater 30, makes this organic gas 13 when carrying out second-time burning, can guarantee that burning is more complete, and produce steam 131 and carbon dioxide 132 simultaneously; This air blast 55 is to be arranged on the body of heater 30, and its air that external world is a large amount of is fed through in the body of heater 30, and this organic gas 13 can quick and completely be burnt, and gets rid of phenomenons such as gas combustion is incomplete fully and produces; This air heat exchanger 56 is to be arranged on the body of heater 30, and it is to heat up after the activation entering cold airs in the body of heater 30 with furnace temperature in advance, makes the oxygen activity in body of heater 30 internal combustion stronger, and then reduces the loss of fuel and increase multinomial gains such as reaction speed; This body of heater cooler 57 is to be arranged on the body of heater 30, and it utilizes heat exchange principle that cooling water and furnace temperature are done heat exchange, reduces the temperature of this body of heater 30; This air scrubbing cooler 58 is that effects such as gas permeation dedusting after the burning and absorption are disposed to the external world again, prevents the generation of secondary pollution; This pressurizer 59 is negative pressure value of utilizing pressure to detect to measure in this body of heater 30, directly control windmill gravitation with pressure controller control frequency converter again, and then reach the effect of balance body of heater 30 internal pressures, and allow this organic gas 13 handle simultaneously according to single direction.Learnt that by above-mentioned this gas smoke consumer 50 can transform steam 131 and carbon dioxide 132 with the organic gas after the thermal cracking 13 really, no any environmentally harmful material is discharged in its process, meets every regulation of environmental protection fully.
Claims (9)
1, a kind of processing method to waste products that brominated epoxy resin and glass fibre are arranged is characterized in that:
This method is that a waste products that contains brominated epoxy resin and glass fibre is fed in the inorganic salts of fusion, make the inorganic salts of this fusion can be directly and the bromine in the brominated epoxy resin produce reaction, and to this waste products generation thermal cracking, separate thereby make this brominated epoxy resin can produce voluntarily, and obtain bromination salt, pure glass fibre and organic gas respectively with glass fibre.Wherein, this organic gas system uses a completing combustion apparatus, will change into the steam and the carbon dioxide of environmental sound after its completing combustion.
2, a kind of processing method to the waste products that contain brominated epoxy resin and glass fibre according to claim 1, it is characterized in that: wherein, these inorganic salts are potassium nitrate.
3, a kind of processing method to the waste products that contain brominated epoxy resin and glass fibre according to claim 1, it is characterized in that: wherein, these inorganic salts are ammonium nitrate.
4, a kind of processing method to the waste products that contain brominated epoxy resin and glass fibre according to claim 1, it is characterized in that: wherein, these inorganic salts are nitrite natrium.
5, a kind of processing method to the waste products that contain brominated epoxy resin and glass fibre according to claim 1, it is characterized in that: wherein, these inorganic salts are that nitric acid is received.
6, a kind of processing method to the waste products that contain brominated epoxy resin and glass fibre according to claim 1 is characterized in that: wherein, these inorganic salts are the two or more mixture during potassium nitrate, ammonium nitrate, nitrite natrium, nitric acid are received.
7, a kind of processing method to the waste products that contain brominated epoxy resin and glass fibre according to claim 1, it is characterized in that: wherein, this organic gas system comprises: hydrogen (H
2), water (H
2O), carbon monoxide (CO), carbon dioxide (CO
2), methane (CH
4), ethane (C
2H
6), the rare (C of second
2H
4), acetylene (C
2H
2), methyl alcohol (CH
3OH), ethanol (C
2H
5OH), C
3(propane, third rare, acetone, propyl alcohol etc.), C
4(butane, fourth are rare, butanone, butanols etc.), C
5, C
6Or the like.
8, a kind for the treatment of apparatus to the waste products that contains brominated epoxy resin and glass fibre, it is to contain the waste products of brominated epoxy resin and glass fibre and the device of the capable thermal cracking of molten salt for this, it is characterized in that: it comprises a body of heater and a heater; Have a feeding mouth on this body of heater, inorganic salts draw off valve, a glass fibre discharging tractor and a discharging opening; Wherein, this feeding mouth system adopts the two door design of external door and inside door.
9, described according to Claim 8 a kind for the treatment of apparatus to the waste products that contains brominated epoxy resin and glass fibre, it is characterized in that: wherein, this treating apparatus comprises that more one is used for the gas smoke consumer of this organic gas of completing combustion, and it has a recirculation reactor, an oxygen enriching burning-aid reactor, air reaction buffering stop device, a post bake burner, an air blast, an air heat exchanger, a body of heater cooler, an air scrubbing cooler and a pressurizer; Wherein, this recirculation reactor system is arranged in this body of heater; This oxygen enriching burning-aid reactor system is arranged in this body of heater; This air reaction buffering stops device system and is arranged in this body of heater; This post bake burner system is arranged on this body of heater; This air blast system is arranged on the body of heater; This air heat exchanger system is arranged on the body of heater; This body of heater cooler system is arranged on the body of heater; This air scrubbing cooler is that effects such as gas permeation dedusting after the burning and absorption are disposed to the external world again, prevents the generation of secondary pollution; This pressurizer is to utilize pressure to detect the negative pressure value of measuring in this body of heater, directly control windmill gravitation with pressure controller control frequency converter again, and then reach the effect of balance body of heater internal pressure, and allow this organic gas handle simultaneously according to single direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03102374 CN1286586C (en) | 2003-02-11 | 2003-02-11 | Method and apparatus for processing waste containing bromination epoxy resin and glass fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03102374 CN1286586C (en) | 2003-02-11 | 2003-02-11 | Method and apparatus for processing waste containing bromination epoxy resin and glass fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1520943A true CN1520943A (en) | 2004-08-18 |
| CN1286586C CN1286586C (en) | 2006-11-29 |
Family
ID=34281687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03102374 Expired - Fee Related CN1286586C (en) | 2003-02-11 | 2003-02-11 | Method and apparatus for processing waste containing bromination epoxy resin and glass fiber |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1286586C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102115547A (en) * | 2010-12-17 | 2011-07-06 | 中国科学院长春应用化学研究所 | Molten bath and method for recycling thermosetting epoxy resin or composite material by using same |
| CN101407596B (en) * | 2008-09-25 | 2011-08-17 | 上海第二工业大学 | Method for recycling epoxy resins and glass fibre from non-metal powder of waste printed circuit board |
| CN101921915B (en) * | 2009-06-12 | 2012-05-23 | 巫协森 | Method and device for recycling substrates by thermally cracking wasted printed circuit boards |
| CN102755987A (en) * | 2012-08-08 | 2012-10-31 | 上海第二工业大学 | Environmental protection recovery method of red mud and abandon bromo flame retardant plastic copyrolysis |
| CN109331776A (en) * | 2018-10-25 | 2019-02-15 | 华中科技大学 | Bromine system flame retardant waste plastic and red mud pyrolysis prepare the method and product of demercuration adsorbent |
-
2003
- 2003-02-11 CN CN 03102374 patent/CN1286586C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101407596B (en) * | 2008-09-25 | 2011-08-17 | 上海第二工业大学 | Method for recycling epoxy resins and glass fibre from non-metal powder of waste printed circuit board |
| CN101921915B (en) * | 2009-06-12 | 2012-05-23 | 巫协森 | Method and device for recycling substrates by thermally cracking wasted printed circuit boards |
| CN102115547A (en) * | 2010-12-17 | 2011-07-06 | 中国科学院长春应用化学研究所 | Molten bath and method for recycling thermosetting epoxy resin or composite material by using same |
| CN102115547B (en) * | 2010-12-17 | 2014-11-12 | 中国科学院长春应用化学研究所 | Molten bath and method for recycling thermosetting epoxy resin or composite material by using same |
| CN102755987A (en) * | 2012-08-08 | 2012-10-31 | 上海第二工业大学 | Environmental protection recovery method of red mud and abandon bromo flame retardant plastic copyrolysis |
| CN109331776A (en) * | 2018-10-25 | 2019-02-15 | 华中科技大学 | Bromine system flame retardant waste plastic and red mud pyrolysis prepare the method and product of demercuration adsorbent |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1286586C (en) | 2006-11-29 |
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