CN202962443U - Process system for preparing diluting agent from industrial waste paint residues - Google Patents
Process system for preparing diluting agent from industrial waste paint residues Download PDFInfo
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- CN202962443U CN202962443U CN 201220565575 CN201220565575U CN202962443U CN 202962443 U CN202962443 U CN 202962443U CN 201220565575 CN201220565575 CN 201220565575 CN 201220565575 U CN201220565575 U CN 201220565575U CN 202962443 U CN202962443 U CN 202962443U
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- heating tank
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Abstract
The utility model discloses a process system for preparing a diluting agent from industrial waste paint residues, and relates to an environment-friendly regeneration recycling device. The process system comprises a heating device system, a reaction device system, a cooling device system, a product discharging and receiving system and a tail gas treatment device system, wherein the heating device system comprises a cooking range; the reaction device system comprises a heating tank; the cooling device system comprises a gas cooling device, a water tower and a condensate water tank; and the tail gas treatment device system comprises a tail gas discharge pipe and a cold chamber. Compared with the prior art, the process system for preparing the diluting agent from the industrial waste paint residues has the advantages that wastes which are generated by a plurality of printing enterprises and cannot be recycled are changed into treasures, so that waste and old resources are reasonably used, energy resources are saved, and pollution, noise and sewage discharge to the surrounding environment, ecology and air are avoided in the whole production process.
Description
Technical field
The utility model relates to a kind of environmental friendly regenerated use device, particularly a kind of process system for preparing diluent for waste painting slag of industry.
Background technology
The manufacturing enterprise that industrial residue is particularly printed the waste residue of industry generally is embedded in these waste residues in earth or burns, and these two kinds of methods have been wasted resource on the one hand, have polluted on the other hand soil and atmosphere, and environment has been brought expendable disaster.
Summary of the invention
For above-mentioned weak point, the purpose of this utility model just is to provide a kind of process system for preparing diluent for waste painting slag of industry, this process system for preparing diluent for waste painting slag of industry can not and can't be processed the industrial residue that relates to environmental pollution in utilization with many printing enterprises at all turns waste into wealth, carry out the reasonable utilization of waste and old resource, and the saving energy, in whole production process to around pollution-free, the noiselessness of environment, ecology and air and discharge without dirt.
The technical solution of the utility model is: a kind of process system for preparing diluent for waste painting slag of industry, described process system comprise that heater system, reaction unit system, chiller system, product discharge receiving system and exhaust gas processing device system; Described heater system comprises cooking stove, and described reaction unit system comprises heating tank, and described chiller system comprises gas quench system, water tower and condensation pond, and described exhaust gas processing device system comprises exhaust emission tube and iced chamber.
As preferably, described cooking stove comprises the cooking stove main body, this cooking stove main body comprises grate, furnace roof, furnace wall and heating tank supporter, lay heating tank on described heating tank supporter, described furnace roof flushes with described heating tank top, spacing h1 between bottom described grate and described heating tank is 50cm, and the spacing h2 between described furnace wall inwall and described heating tank outer wall is 30cm.
As preferably, also be provided with finalization area between described furnace roof and described heating tank roof, this finalization area spacing h3 is 2cm.
As preferably, described heating tank comprises lid, industrial residue district and gas compartment district, is provided with gas flow on described lid and portals.
As preferably, the ratio in described industrial residue district and described gas compartment district is less than or equal to 2.
As preferably, described gas quench system comprises that gas flows out vertical tube, tube connector and gas cooling tube, and the outer coaxial sleeve of described gas cooled pipe has the water-setting pipe, and described gas cooled pipe and described water-setting tubular axis line level are slightly downward-sloping; Described water-setting pipe lower end is connected with water inlet pipe, and the upper end is connected with outlet pipe; Described water-setting pipe shell port and described gas cooled pipe shell are by the plumb joint end socket; Described water-setting pipe diameter is the twice of described gas cooled pipe diameter; Described gas flows out vertical tube, tube connector is identical with gas cooling tube diameter, and described gas flows out the angle of vertical tube and gas cooled Guan Suocheng less than 90 degree.
As preferably, it is that 40cm, diameter are 5cm that described gas flows out the vertical tube pipe range, and the tube connector pipe range is that 40 cm, diameter are 5cm, and gas cooled pipe pipe range is that 10.5m, diameter are 5cm, and water-setting pipe pipe range is that 10m, diameter are 10cm; Distance between described water-setting pipe upper port and described gas cooled pipe upper port is 25cm, and the distance between described water-setting infratubal port and described gas cooled infratubal port is 25cm; Distance between described water inlet pipe and described water-setting infratubal port is 20cm, and the distance between described outlet pipe and described water-setting pipe upper port is 20cm, and described water inlet pipe diameter is that 3cm, length are 40cm, and described diameter of outflow tube is that 3cm, length are 40cm.
As preferably, described product is discharged receiving system and is comprised that diluent flows out pipe and product receiving tank, and described diluent outflow pipe is arranged on directly over the product receiving tank.
As preferably, described iced chamber is comprised of adiabator layer, insulation material layer and damp-proof layer, and described adiabator layer is the polyurethane spray coating foaming material of thick 10cm, and described damp-proof layer is the solidifying S52-1 polyurethane cyanogen gel material of cyanogen.
As preferably, described reaction unit system, chiller system and product are discharged receiving system and are all adopted stainless steel to make.
Compared with prior art, the beneficial effects of the utility model are:
1) many printing enterprises can not and can't be processed the industrial residue that relates to environmental pollution in utilization at all turns waste into wealth, carry out the reasonable utilization of waste and old resource, and the saving energy, in whole production process to around pollution-free, the noiselessness of environment, ecology and air and discharge without dirt.
2) liquid diluent that flows out can not enter exhaust emission tube
3) temperature due to gas compartment district is controlled at below 150 ℃, and because diluent flows out pipe, exhaust emission tube is identical with cooling tube rear diameter, and diluent flows out pipe and becomes miter angle with the cooling tube rear, therefore when liquid diluent inflow diluent outflow pipe splashes into the product receiving tank again, extraneous air enters simultaneously, thereby make the pressure in whole diluent preparation system keep balance, therefore the heating tank in the diluent preparation system can be because pressure imbalance explodes, therefore can not burn in production process, can not explode, without any potential safety hazard.
Description of drawings
Fig. 1 is overall structure schematic diagram of the present utility model;
Fig. 2 is the tube connector schematic diagram that heating tank of the present utility model and gas flow out vertical tube;
Fig. 3 is iced chamber overall structure schematic diagram of the present utility model.
The specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
As Figure 1-3 be used for the process system that waste painting slag of industry prepares diluent, this process system comprises that heater system, reaction unit system, chiller system, product discharge receiving system and exhaust gas processing device system.
The heater system comprises cooking stove 1, and the reaction unit system comprises heating tank 2.Cooking stove 1 comprises grate 5, furnace roof, furnace wall and heating tank supporter 3, lay heating tank 2 on heating tank supporter 3, furnace roof flushes with heating tank 2 tops, and the spacing h1 between grate 5 and heating tank 2 bottoms is 50cm, and the spacing h2 between furnace wall inwall and described heating tank 2 outer walls is 30cm.Also be provided with finalization area 6 between furnace roof and heating tank 2 roofs, this finalization area 6 spacing h3 are 2cm, and finalization area 6 closed materials adopt earth and water.Finalization area 6 spacing h3 are that 2cm can make sealing operation easy on the one hand, also can reach good sealing effect on the other hand.Cooking stove 1 can be square or cylindrical shape, and heating tank 2 can be square, cylindrical shape or taper.
Cooking stove 1 is placed in heating tank supporter 3 with heating tank 2 after substantially being built into (finalization area 6 is not built), then with the band soil cement after mixing, finalization area 6 is filled up, and whole block furnaceman skill is completed after earth is done.
Heating tank 2 comprises lid, industrial residue district 21 and gas compartment district 22.Be provided with gas flow on lid and portal, gas is installed on gas flow portals flows out vertical tube 7, gas flows out vertical tube 7 and is connected by tube connector 24 with lid, and tube connector 24 comprises tapped outer tube and is with externally threaded inner tube.Gas flow portal can for one, more than 2 or 3, it is 2 the bests that gas flow portals, because if it is 1 that excessive gas flow portals, the overall throughput of producing is less, be unfavorable for improving production capacity and energy savings, gas flow portals and is more than 3 can affects the sealing of heating tank if overflow, and it is 2 sealings that can take into account well production production capacity and heating tank that the gas flow that overflows portals.Heating also is provided with a thermometer on tank body, and thermometer is used for the temperature in monitoring gas compartment district 22.The ratio in industrial residue district 21 and gas compartment district 22 is less than or equal to 2, and ratio equals 2 can reach best using energy source and integral production production capacity.Heating tank 2 is sealed shell of tank, and lid compresses by bolt.
Chiller system comprises gas quench system, water tower 21 and condensation pond 22.The height of water tower 21 need exceed cooking stove 1 4-5 rice, and condensation pond 22 is built on the ground, and size is about 100 cubes, and the water in water tower 21 and condensation pond 22 is distilled water, provides gas quench system required cooling water.
Gas quench system comprises that gas flows out vertical tube 7, tube connector 8 and gas cooling tube 9, and the outer coaxial sleeve of gas cooled pipe 9 has water-setting pipe 10, and gas cooled pipe 9 is slightly downward-sloping with water-setting pipe 10 axis horizontal.Water-setting pipe 10 lower ends are connected with water inlet pipe 11, and the upper end is connected with outlet pipe 12, and water-setting pipe 10 outer cover ports and gas cooled pipe 9 shells are by plumb joint 13 end sockets.Water-setting pipe 10 diameters are the twice of gas cooled pipe 9 diameters, and gas flows out vertical tube 7, tube connector 8 is identical with gas cooling tube 9 diameters.Gas flows out the angle of vertical tube 7 and 9 one-tenth of gas cooled pipes less than 90 degree, and angle is 75 to spend the dilution dosage that can reach best and best diluent.It is that 40cm, diameter are 5cm that gas flows out vertical tube 7 pipe ranges, and tube connector 8 pipe ranges are that 40 cm, diameter are 5cm, and gas cooled pipe 9 pipe ranges are that 10.5m, diameter are 5cm, and water-setting pipe 10 pipe ranges are that 10m, diameter are 10cm.Distance between water-setting pipe 10 upper port and gas cooled pipe 9 upper port is 25cm, and the distance between water-setting pipe 10 lower port and gas cooled pipe 9 lower port is 25cm.Distance between water inlet pipe 11 and water-setting pipe 10 lower port is 20cm, and the distance between outlet pipe 12 and water-setting pipe 10 upper port is 20cm, and water inlet pipe 11 diameters are that 3cm, length are 40cm, and outlet pipe 12 diameters are that 3cm, length are 40cm.Adopt these sizes can reach on the one hand best dilution dosage and best diluent, can save required pipeline material on the one hand, energy resource consumption simultaneously is low, can save the energy.Gas flows out vertical tube 7, tube connector 8, gas cooled pipe 9, water-setting pipe 10, water inlet pipe 11 and outlet pipe 12 and all adopts the stainless steel steel, adopts the stainless steel steel can make diluent and the cooling water produced not contain yellow impurities.
Gas flows out the movable bolt of vertical tube 7 use and is connected on the lid of heating tank 2.
Product is discharged receiving system and is comprised that diluent flows out pipe 14 and product receiving tank 15, and the exhaust gas processing device system comprises exhaust emission tube 19, condenser coil 201, liquid effuser 202, liquid receiving tank 203, exhaust emission tube 204 and iced chamber 20.Product receiving tank 15 is arranged on diluent and flows out under pipe 14, and diluent flows out pipe 14 and 9 one-tenth miter angles of gas cooled pipe.Exhaust emission tube 16 is divided into three section 19 of a section 17 of exhaust emission tube, two section 18 of exhaust emission tube and exhaust emission tube, one section 17 of exhaust emission tube and gas cooled pipe 9 are in line, exhaust emission tube becomes miter angle with horizontal line for two section 18, and exhaust emission tube becomes for three section 19 0 to spend the angle with horizontal line.Diluent flows out pipe 14, one section 17 of exhaust emission tube, two section 18 of exhaust emission tube and three section 19 diameter of exhaust emission tube and is 5cm.Product receiving tank 15 can be for square, circular or irregularly shaped.Condenser coil 201 is arranged in iced chamber 20, and liquid effuser 202 is connected with exhaust emission tube and is connected respectively condenser coil 201, and liquid receiving tank 203 and exhaust emission tube 204 lead to respectively outside iced chamber 20, and liquid receiving tank 203 bottoms are provided with valve.Iced chamber 20 temperature are controlled at subzero 10 degree.The liquid receiving tank can be one, also can be two.Iced chamber 20 is comprised of adiabator layer 3, insulation material layer 5 and damp-proof layer 4, and adiabator layer 3 is the polyurethane spray coating foaming material of thick 10cm, and damp-proof layer 4 is the solidifying S52-1 polyurethane cyanogen gel material of cyanogen.
During production, coal-fired in burner hearth 4 internal combustion, because the spacing h2 between furnace wall inwall and described heating tank 2 outer walls is 30cm, therefore burned flame can fully surround heating tank 2 on the one hand, heating tank 2 is heated even as far as possible, the heat energy of burning generation can reduce the suffered heat energy of each single-point of heating tank 2 because the space is too large on the other hand.Waste painting slag of industry in heating tank 2 is evaporated to gas after being heated and dissolving, and the temperature in gas compartment district 22 is controlled at below 150 ℃.Nearly 100 ℃ the time, open the valve of water inlet pipe 11 when the temperature in gas compartment district 22, pass into cooling water, carry out cooling to gas cooled pipe 9.
From heating tank 2 out gas enter gas flow out enter after vertical tube 7, tube connector 8 carry out in gas cooled pipe 9 cooling, adopt the cooling water of distilled water to carry out heat exchange from the gas that water inlet pipe 11 enters water-setting pipe 10 and gas cooled pipe 9, hot water after exchange is gone out from the outlet pipe 12 of upper end, and the gas temperature that gas cooled pipe 9 is exported is controlled at 25 ℃.Because cooling water adopts distilled water, so can not produce incrustation scale in water-setting pipe 10, can not produce harmful effect to heat exchange, cooling water can recycle in water-setting pipe 10, water tower 21 and condensation pond 22.Liquid from gas cooled pipe 9 gas-liquid mixture out flows into diluent outflow pipe 14 and then splashes into product receiving tank 15, and gas enters exhaust emission tube 16.Enter iced chamber 20 from the tail gas of exhaust emission tube 19 and carry out condensation, condensed liquid enters liquid receiving tank 203, fills rear taking-up until liquid receiving tank 203.Tail gas condensing liquid also can be used as diluent and uses.
After producing end, have a small amount of waste painting slag of industry recrement to become black crystals shape, free from extraneous odour in heating tank 2, this a small amount of waste painting slag of industry recrement can be used as the fuel combustion in burner hearth 4.
If adopt coal as the fuel of heating tank 2 in production, the burning gases that produce and flue dust can be transported to purification water pool 23 by pipeline and carry out water treatment, purification water pool 23 is totally enclosed type, volume is 300 cubes, purification water pool 23 adopts waterproof material, have a steam vent on purification water pool 23, on this steam vent, discharge duct is housed.Water in purification water pool 23 uses for a long time.
Claims (10)
1. one kind is used for the process system that waste painting slag of industry prepares diluent, it is characterized in that: described process system comprises that heater system, reaction unit system, chiller system, product discharge receiving system and exhaust gas processing device system; Described heater system comprises cooking stove, and described reaction unit system comprises heating tank, and described chiller system comprises gas quench system, water tower and condensation pond, and described exhaust gas processing device system comprises exhaust emission tube and iced chamber.
2. the process system for preparing diluent for waste painting slag of industry according to claim 1, it is characterized in that: described cooking stove comprises the cooking stove main body, this cooking stove main body comprises grate, furnace roof, furnace wall and heating tank supporter, lay heating tank on described heating tank supporter, described furnace roof flushes with described heating tank top, spacing h1 between bottom described grate and described heating tank is 50cm, and the spacing h2 between described furnace wall inwall and described heating tank outer wall is 30cm.
3. the process system for preparing diluent for waste painting slag of industry according to claim 2, it is characterized in that: also be provided with finalization area between described furnace roof and described heating tank roof, this finalization area spacing h3 is 2cm.
4. the process system for preparing diluent for waste painting slag of industry according to claim 1 is characterized in that: described heating tank comprises lid, industrial residue district and gas compartment district, is provided with gas flow on described lid and portals.
5. the process system for preparing diluent for waste painting slag of industry according to claim 4 is characterized in that: the ratio in described industrial residue district and described gas compartment district is less than or equal to 2.
6. the process system for preparing diluent for waste painting slag of industry according to claim 1, it is characterized in that: described gas quench system comprises that gas flows out vertical tube, tube connector and gas cooling tube, the outer coaxial sleeve of described gas cooled pipe has the water-setting pipe, and described gas cooled pipe and described water-setting tubular axis line level are slightly downward-sloping; Described water-setting pipe lower end is connected with water inlet pipe, and the upper end is connected with outlet pipe; Described water-setting pipe shell port and described gas cooled pipe shell are by the plumb joint end socket; Described water-setting pipe diameter is the twice of described gas cooled pipe diameter; Described gas flows out vertical tube, tube connector is identical with gas cooling tube diameter, and described gas flows out the angle of vertical tube and gas cooled Guan Suocheng less than 90 degree.
7. the process system for preparing diluent for waste painting slag of industry according to claim 6, it is characterized in that: it is that 40cm, diameter are 5cm that described gas flows out the vertical tube pipe range, the tube connector pipe range is that 40 cm, diameter are 5cm, gas cooled pipe pipe range is that 10.5m, diameter are 5cm, and water-setting pipe pipe range is that 10m, diameter are 10cm; Distance between described water-setting pipe upper port and described gas cooled pipe upper port is 25cm, and the distance between described water-setting infratubal port and described gas cooled infratubal port is 25cm; Distance between described water inlet pipe and described water-setting infratubal port is 20cm, and the distance between described outlet pipe and described water-setting pipe upper port is 20cm, and described water inlet pipe diameter is that 3cm, length are 40cm, and described diameter of outflow tube is that 3cm, length are 40cm.
8. the process system for preparing diluent for waste painting slag of industry according to claim 1 is characterized in that: described product is discharged receiving system and is comprised that diluent flows out pipe and product receiving tank, and described diluent outflow pipe is arranged on directly over the product receiving tank.
9. the process system for preparing diluent for waste painting slag of industry according to claim 1, it is characterized in that: described iced chamber is comprised of adiabator layer, insulation material layer and damp-proof layer, described adiabator layer is the polyurethane spray coating foaming material of thick 10cm, and described damp-proof layer is the solidifying S52-1 polyurethane cyanogen gel material of cyanogen.
10. the process system for preparing diluent for waste painting slag of industry according to claim 1 is characterized in that: described reaction unit system, chiller system and product are discharged receiving system and are all adopted stainless steel to make.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220565575 CN202962443U (en) | 2012-10-31 | 2012-10-31 | Process system for preparing diluting agent from industrial waste paint residues |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220565575 CN202962443U (en) | 2012-10-31 | 2012-10-31 | Process system for preparing diluting agent from industrial waste paint residues |
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| Publication Number | Publication Date |
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| CN202962443U true CN202962443U (en) | 2013-06-05 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201220565575 Expired - Fee Related CN202962443U (en) | 2012-10-31 | 2012-10-31 | Process system for preparing diluting agent from industrial waste paint residues |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021142657A1 (en) * | 2020-01-15 | 2021-07-22 | 杰瑞环保科技有限公司 | Thermal phase separation treatment process for paint waste residue and apparatus thereof |
-
2012
- 2012-10-31 CN CN 201220565575 patent/CN202962443U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021142657A1 (en) * | 2020-01-15 | 2021-07-22 | 杰瑞环保科技有限公司 | Thermal phase separation treatment process for paint waste residue and apparatus thereof |
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Legal Events
| Date | Code | Title | Description |
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| 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: 20130605 Termination date: 20151031 |
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| EXPY | Termination of patent right or utility model |