CN103433266A - Intelligent reaction kettle equipment system for industrial wastes - Google Patents
Intelligent reaction kettle equipment system for industrial wastes Download PDFInfo
- Publication number
- CN103433266A CN103433266A CN2013101087652A CN201310108765A CN103433266A CN 103433266 A CN103433266 A CN 103433266A CN 2013101087652 A CN2013101087652 A CN 2013101087652A CN 201310108765 A CN201310108765 A CN 201310108765A CN 103433266 A CN103433266 A CN 103433266A
- Authority
- CN
- China
- Prior art keywords
- kettle
- still
- hthp
- stirring
- rib
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Images
Abstract
The invention discloses an intelligent reaction kettle equipment system for industrial wastes. The intelligent reaction kettle equipment system comprises a crusher, a plate type feeding machine and a high temperature and high pressure rotating reaction kettle which are arranged successively. The high temperature and high pressure rotating reaction kettle is provided with a pressure sensor, a temperature sensor and a humidity sensor respectively for measuring reaction pressure, temperature and humidity in an inner cavity during an industrial solid waste reaction process. The high temperature and high pressure rotating reaction kettle is also communicated with an exhaust pipe. One side of the high temperature and high pressure rotating reaction kettle is provided with an intelligent control center for controlling work of the high temperature and high pressure rotating reaction kettle according to data feedback by the pressure sensor, the temperature sensor and the humidity sensor. The high temperature and high pressure rotating reaction kettle is also provided with a steam adjusting valve controlled by the intelligent control center.
Description
[technical field]
The present invention relates to the treatment facility of trade waste, relate in particular to intelligent trade waste reactor device systems.
[background technology]
Energy problem is one of deciding factor affected socio-economic development, solve energy problem and just solved the dynamical problem of economic development, the conventional energy resource of China is in short supply has had a strong impact on socioeconomic fast development, and fossil energy is concentrated and is used on a large scale, discharge the materials such as great amount of carbon dioxide, sulfur dioxide, nitrogen oxide, caused harm to the mankind's living environment, countries in the world are all strengthened the developmental research of renewable energy technologies energetically for this reason.
The calorific values such as vinasse, the dregs of a decoction, offal, paper mud are higher but trade waste that viscosity is lower, occupy critical role in regenerative resource, the shortage that the exploitation trade waste supplements conventional energy resource as biomass energy, by the calorific values such as vinasse, the dregs of a decoction, offal, paper mud are higher but the trade waste that viscosity is lower even danger wastes carry out innoxious, energy and process, realize the resource maximum using, there is great environmental benefit.
[summary of the invention]
The present invention utilizes automatic feed/discharge control device and automatic vent voltage-regulating technique, provide a kind of automaticity high, can realize virus killing, sterilizing and deodorization functions, can modularization, the intelligent trade waste reactor device systems of industrialization, innoxious, resource, energy.
In order to realize goal of the invention of the present invention, the technical scheme of employing is:
Intelligent trade waste reactor device systems, comprise the disintegrating machine be arranged in order, apron feeder and HTHP revolving reaction still, be respectively arranged with on HTHP revolving reaction still and measure pressure in inner chamber Industrial Solid Waste course of reaction, the pressure sensor of temperature and humidity, temperature sensor and humidity sensor, also be communicated with offgas duct on HTHP revolving reaction still, in HTHP revolving reaction still one side, also be provided with according to pressure sensor, the intelligent control center of the Data Control HTHP revolving reaction still work of temperature sensor and humidity sensor feedback, also be provided with the steam control valve of being controlled by intelligent control center on HTHP revolving reaction still.
Intelligent trade waste reactor device systems, also be connected with the biological treatment device that high-temperature vapor to discharging carries out condensation separating unit, the device for absorbing tail gas that the inorganic gas in tail gas is absorbed of condensation separation and tail gas carried out to organic process in turn on the offgas duct of described HTHP revolving reaction still.
Intelligent trade waste reactor device systems as above, HTHP revolving reaction still comprises kettle; Kettle comprises heat-insulation layer, still wall, and heat-insulation layer is in still wall outside; The still wall stretches into and forms a plurality of stirring ribs to inner chamber, and stirring the rib height is 1/4 to 1/2 of kettle radius, in still wall and stirring rib, is provided with heat pipe.
Intelligent trade waste reactor device systems as above, HTHP revolving reaction still comprises kettle; Kettle comprises heat-insulation layer, still wall, and heat-insulation layer is in still wall outside; The still wall stretches into and forms a plurality of stirring ribs to inner chamber, and stirring the rib height is 1/4 to 1/2 of kettle radius, and the inboard of still wall is provided with heat pipe.
Intelligent trade waste reactor device systems as above, HTHP revolving reaction still comprises kettle; Kettle comprises heat-insulation layer, still wall, and heat-insulation layer is in still wall outside; The still wall stretches into and forms a plurality of stirring ribs to inner chamber, and stirring the rib height is 1/4 to 1/2 of kettle radius, and still wall and stirring in rib is provided with the mobile cavity for superheated vapour of one.
Intelligent trade waste reactor device systems as above, the axial angle α span of described stirring rib and kettle rotating shaft is 20～30 °, and cross section the above stirring rib and the kettle angle β span in the radial direction axial perpendicular to rotating shaft at kettle are 5～15 °.
Intelligent trade waste reactor device systems as above, the tubbiness rotary body that described kettle is horizontal inclined placement, be provided with in the heart material exchange mouthful in kettle inner cone lid, material exchange mouth is provided with to reinforced feeding device in kettle, and feeding device is provided with loading hopper and the dump skip be connected with material exchange mouth; Described kettle front and back ends is provided with the forward and backward carrier base that supports its rotation; The kettle downside is provided with the power set that drive kettle to rotate.
Intelligent trade waste reactor device systems as above, described still wall is along circumferentially being divided into a plurality of heating intervals, the axial coil pipe formed after each heating interval inner heat-conductive pipe series connection is communicated with respectively with the swivel joint that the kettle rear end arranges, heat pipe in each heating interval is connected with the input flexible pipe of setting by swivel joint, and the heat pipe in each heating interval also is connected with the delivery hose of setting by swivel joint; Be provided with the thermal source section that supplies with conduction oil to heat pipe at the kettle rear side, the output of thermal source section is connected with separator, the input of thermal source section is connected with oil catcher, all input flexible pipes are communicated with separator is in parallel, all delivery hoses and oil catcher are in parallel to be communicated with, the soft circulation circuit of described thermal source section, separator, input flexible pipe, swivel joint, heat pipe, delivery hose and a sealing of oil catcher formation.
Intelligent trade waste reactor device systems as above, described still wall and the cavity stirred in rib are communicated with a swivel joint, this swivel joint is connected with the input flexible pipe, be provided with and supply with the thermal source section of superheated vapour by the input flexible pipe to still wall and the cavity in the stirring rib at the kettle rear side, also be provided with on kettle with still wall and the cavity stirred in rib and be communicated with the drain valve of being convenient to condensed water discharge in cavity.
Intelligent trade waste reactor device systems as above, described power set comprise electromagnetic adjustable speed motor and reduction box, between electromagnetic adjustable speed motor and reduction box, by belt pulley, be connected, on the output shaft of reduction box, pinion is installed, corresponding upwards is provided with the gear wheel coordinated with pinion in kettle wall week.
Compared with prior art, the present invention has following advantage:
The power set that the present invention arranges by HTHP revolving reaction still kettle downside, can control HTHP revolving reaction still input and output material automatically, in whole course of reaction, HTHP revolving reaction still passes through intelligent control center, according to pressure sensor, the pressure of the kettle inner chamber Industrial Solid Waste that temperature sensor and humidity sensor are surveyed, temperature and humidity, the work of control steam control valve, and then the soft circulation circuit formed by intelligent control center control of heat source section, constantly to the Industrial Solid Waste heating and dehumidification in HTHP revolving reaction still, reach on-line monitoring HTHP revolving reaction still, realize boosting of intelligence, voltage stabilizing and unload pressure-controlled, by the HTHP in HTHP revolving reaction still, the Industrial Solid Waste in it is killed virus, sterilizing and deodorizing, realization is to the trade waste energy, innoxious and recycling treatment,
Simultaneously, the offgas duct of HTHP revolving reaction still is connected with condensation separating unit, device for absorbing tail gas and biological treatment device in turn, after can carrying out condensation process to the high-temperature vapor of discharging, recycle condensed water, and can the organic and inorganic gas in tail gas be absorbed, realize that tail gas focuses on, reach modularization, industrialization, intellectuality (automatic feed/discharge, the automatic vent pressure regulation) management, and realize innoxious, resource and the energy of Industrial Solid Waste fuel.
In addition, the kettle wall of HTHP revolving reaction still stretches into and forms a plurality of stirring ribs to the kettle inner chamber, increase the still wall and stirred rib and kettle inner chamber internal layer Industrial Solid Waste contact area, the heating surface area of Industrial Solid Waste in kettle is increased, utilization efficiency of heat energy improves, the stirring rib simultaneously be obliquely installed can also be stirred Industrial Solid Waste, and the Industrial Solid Waste in kettle is heated evenly; And adopt same material exchange mouthful to adding the output of material after Industrial Solid Waste and processing in kettle, and reduced the use of kettle water-tight equipment, reduced technical costs.
[accompanying drawing explanation]
Fig. 1 is system architecture schematic diagram of the present invention;
Fig. 2 is the main TV structure schematic diagram of HTHP revolving reaction still embodiment mono-in the present invention;
Fig. 3 is the side-looking structural representation of Fig. 2;
Fig. 4 is the plan structure schematic diagram of Fig. 2;
Fig. 5 is the kettle sectional structure schematic diagram of HTHP revolving reaction still embodiment mono-in the present invention;
Fig. 6 is the kettle cross section structure schematic diagram of HTHP revolving reaction still embodiment mono-in the present invention;
Fig. 7 is the cross section structure schematic diagram of the kettle of HTHP revolving reaction still embodiment bis-in the present invention;
Fig. 8 is the main TV structure schematic diagram of HTHP revolving reaction still embodiment tri-in the present invention;
Fig. 9 is the side-looking structural representation of Fig. 8;
Figure 10 is the cross section structure schematic diagram of the kettle of HTHP revolving reaction still embodiment tri-in the present invention.
[specific embodiment]
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is clearly and completely described, obviously, described embodiment is only the present invention's part embodiment, rather than whole embodiment.
Intelligent trade waste reactor device systems, as shown in Figure 1, comprise the disintegrating machine a be arranged in order, apron feeder b and HTHP revolving reaction still c, be respectively arranged with on HTHP revolving reaction still c and measure pressure in inner chamber Industrial Solid Waste course of reaction, the pressure sensor c1 of temperature and humidity, temperature sensor c2 and humidity sensor c3, also be communicated with offgas duct c4 on HTHP revolving reaction still c, in HTHP revolving reaction still c mono-side, also be provided with according to pressure sensor c1, the intelligent control center f of the Data Control HTHP revolving reaction still c work of temperature sensor c2 and humidity sensor c3 feedback, also be provided with the steam control valve c5 controlled by intelligent control center f on HTHP revolving reaction still c.
Continue as shown in Figure 1, the offgas duct c4 of HTHP revolving reaction still c is connected with condensation separating unit g, device for absorbing tail gas e and biological treatment device h in turn, condensation separating unit g can carry out condensation process to the high-temperature vapor of discharging, and can be to the utilization of condensed water after processing; Device for absorbing tail gas e absorbs by acid, alkali the inorganic gas of removing in tail gas, and residue VOC gas enters biological treatment device h, realizes the harmless treatment to tail gas.
The HTHP revolving reaction still c mono-that the present invention adopts has three kinds of versions, as follows:
Embodiment mono-
As shown in Figures 2 to 6, the kettle 1 of HTHP revolving reaction still c comprises heat-insulation layer 1a and still wall 1b, the outer wall of heat-insulation layer 1a in kettle 1, still wall 1b is positioned at the inboard of kettle 1 and stretches into and form a plurality of stirring ribs 6 that evenly are provided for increase and kettle inner chamber internal layer material contact area and are convenient to stir Industrial Solid Waste to the kettle inner chamber, stir rib 6 and be multistage distribution straggly, stirring the rib height is 1/3 of kettle radius, the setting party of all stirring ribs 6 to consistent and with axial in a certain angle the arranging of kettle rotating shaft, wherein, stirring the axial angle α span of rib 6 and kettle 1 rotating shaft is 20～30 °, cross section the above stirring rib 6 axial perpendicular to rotating shaft at kettle 1 is 5～15 ° with kettle 1 angle β span in the radial direction.
Continue as shown in Figures 2 to 6, kettle 1 front and back are provided with the forward and backward carrier base (2,3) that supports its rotation, fore-stock seat 2 is provided with two rollers 20, and corresponding kettle 1 wall is provided with the raceway 21 coordinated with all rollers 20, and kettle 1 downside is provided with the power set 4 that drive kettle to rotate; The tubbiness rotary body that kettle 1 is horizontal inclined placement, be provided with in the heart a material exchange mouth 5 of being convenient to the rear material output of the interior interpolation Industrial Solid Waste of kettle 1 and processing in kettle 1 inner cone lid, exchange mouthfuls 5 by material during kettle 1 forward and add materials in kettle 1, during kettle 1 reversion, kettle 1 exchange mouthfuls 5 by material the rear materials of processing is outwards exported.
Continue as shown in Figures 1 to 5, at still wall 1b and stir that rib 6 is interior axially evenly is placed with the many heat pipes that heated for the Industrial Solid Waste to the kettle inner chamber 7 along kettle 1, still wall 1b in described kettle 1 is along circumferentially being divided into a plurality of heating intervals, the axial coil pipe formed after each heating interval inner heat-conductive pipe 7 series connection is communicated with respectively with the swivel joint 8 that kettle 1 rear end arranges, heat pipe 7 in each heating interval also is provided with by swivel joint 8 and is connected with the input flexible pipe 9 of heat-conducting medium input respectively, heat pipe 7 in each heating interval also is provided with by swivel joint 8 and is connected with the delivery hose 10 of heat-conducting medium output respectively, also be provided with thermal source section (not shown) from high temperature heat conducting medium to heat pipe 7 that supply with at kettle 1 rear side, in this embodiment, the heat-conducting medium of thermal source section is conduction oil, the output of thermal source section is connected with separator 11, the input of thermal source section is connected with oil catcher 12, all input flexible pipes 9 are communicated with separator 11 is in parallel, all delivery hoses 10 and oil catcher 12 is in parallel to be communicated with, and described thermal source section, separator 11, input flexible pipe 10, swivel joint 8, heat pipe 7, delivery hose 10 and oil catcher 12 form the soft circulation circuit that a sealing is heated Industrial Solid Waste in kettle.
Continue as shown in Figures 2 to 6, power set 4 comprise electromagnetic adjustable speed motor 40 and reduction box 41, between electromagnetic adjustable speed motor 40 and reduction box 41, by belt pulley 42, be connected, pinion 43 is installed, the corresponding gear wheel 44 coordinated with pinion 41 that upwards is provided with in kettle wall week on the output shaft of reduction box 41.Wherein, also be provided with Pressure gauge 13 on kettle 1; Material exchange mouthful 5 places of kettle 1 also are provided with the feeding device 14 that adds Industrial Solid Waste or microorganism to the kettle inner chamber.
Embodiment bis-
Be the setting of heat pipe with embodiment mono-difference, as shown in Figure 7, the still wall 1b of kettle 1 stretches into and forms a plurality of stirring ribs 6 that evenly are provided for increase and kettle inner chamber internal layer Industrial Solid Waste contact area and are convenient to stir Industrial Solid Waste to kettle 1 inner chamber, stirring the rib height is 1/3 of kettle radius, still wall 1b and stirring rib 6 outsides axially evenly are placed with the many heat pipes 7 that directly with the Industrial Solid Waste of kettle 1 inner chamber, contact heating along kettle 1, and the heat pipe in kettle 17 is along circumferentially being divided into a plurality of heating intervals, the axial coil pipe formed after each heating interval inner heat-conductive pipe 7 series connection is communicated with respectively with the swivel joint 8 that kettle 1 rear end arranges, with structure shown in Fig. 6 in embodiment mono-, compare, when working, the heat pipe 7 in embodiment bis-directly contacts with the Industrial Solid Waste in kettle 1, heating effect is better, other structural configuration are identical with embodiment mono-, do not do too much and repeat at this.
Embodiment tri-
With embodiment mono-difference, be, as shown in Fig. 8 to Figure 10, still wall 1b and stirring in rib 6 is provided with the mobile cavity X for superheated vapour of one, still wall 1b and the cavity X stirred in rib 6 are communicated with a swivel joint 8a, this swivel joint Y is connected with input flexible pipe 10a, be provided with and supply with the thermal source section of superheated vapour by input flexible pipe 10a to the cavity X in still wall 1b and stirring rib 6 at the kettle rear side, in this embodiment, the heat-conducting medium of thermal source section (not shown) is superheated steam, also be provided with on kettle with the cavity X in still wall 1b and stirring rib 6 and be communicated with the drain valve 15 of being convenient to condensed water discharge in cavity.
When this intellectuality trade waste reactor device systems is used, first to solid waste, carry out innoxious, energy is processed, solid waste is after disintegrating machine a processes, through apron feeder b, transmit, exchanging mouthfuls 5 by the loading hopper 140 of feeding device 14 by material adds in the HTHP revolving reaction still c of forward, under the intelligent control of intelligent control center f, HTHP revolving reaction still c boosts, approximately 40 minutes pressure rising time, while reaching the temperature range of 190 °～230 °, HTHP revolving reaction still c enters the automatic constant pressure control process, constant voltage time is about 80 minutes, in constant voltage process, by the HTHP in kettle, trade waste is killed virus, sterilizing and deodorizing, dry control by intelligence, reach the trade waste energy, innoxious and recycling treatment, after constant voltage time, steam off control valve c5, HTHP revolving reaction still c automatically unloading, after release completes, by power set 4, automatically control kettle 1 reversion, from material exchange mouthful 5 automatic dischargings, the dump skip 141 from feeding device 14 is discharged, and can obtain the fuel of solid waste environmental protection.
In the solid waste course of reaction, steam, VOC gas and other gas enter condensation separating unit g by offgas duct c4, at first make gas-water separation, and the condensed water of generation recycles after treatment; Then, device for absorbing tail gas e absorbs by acid, alkali the inorganic gas of removing in tail gas; Residue VOC gas enters biological treatment device h, realizes the harmless treatment to tail gas.
The above embodiment just, for preferred embodiment of the present invention, not limits practical range of the present invention with this; The equivalence that all shapes according to the present invention, structure and principle are done changes, and those of ordinary skills, not making under the creative work prerequisite the every other embodiment obtained, all should be covered by protection scope of the present invention.
Claims (10)
1. intelligent trade waste reactor device systems is characterized in that:
Comprise the disintegrating machine be arranged in order, apron feeder and HTHP revolving reaction still, be respectively arranged with on HTHP revolving reaction still and measure pressure in inner chamber Industrial Solid Waste course of reaction, the pressure sensor of temperature and humidity, temperature sensor and humidity sensor, also be communicated with offgas duct on HTHP revolving reaction still, in HTHP revolving reaction still one side, also be provided with according to pressure sensor, the intelligent control center of the Data Control HTHP revolving reaction still work of temperature sensor and humidity sensor feedback, also be provided with the steam control valve of being controlled by intelligent control center on HTHP revolving reaction still.
2. intelligent trade waste reactor device systems according to claim 1, it is characterized in that, also be connected with the biological treatment device that high-temperature vapor to discharging carries out condensation separating unit, the device for absorbing tail gas that the inorganic gas in tail gas is absorbed of condensation separation and tail gas carried out to organic process on the offgas duct of described HTHP revolving reaction still in turn.
3. intelligent trade waste reactor device systems according to claim 1 and 2, is characterized in that, HTHP revolving reaction still comprises kettle; Kettle comprises heat-insulation layer, still wall, and heat-insulation layer is in still wall outside; The still wall stretches into and forms a plurality of stirring ribs to inner chamber, and stirring the rib height is 1/4 to 1/2 of kettle radius, in still wall and stirring rib, is provided with heat pipe.
4. intelligent trade waste reactor device systems according to claim 1 and 2, is characterized in that, HTHP revolving reaction still comprises kettle; Kettle comprises heat-insulation layer, still wall, and heat-insulation layer is in still wall outside; The still wall stretches into and forms a plurality of stirring ribs to inner chamber, and stirring the rib height is 1/4 to 1/2 of kettle radius, and the inboard of still wall is provided with heat pipe.
5. intelligent trade waste reactor device systems according to claim 1 and 2, is characterized in that, HTHP revolving reaction still comprises kettle; Kettle comprises heat-insulation layer, still wall, and heat-insulation layer is in still wall outside; The still wall stretches into and forms a plurality of stirring ribs to inner chamber, and stirring the rib height is 1/4 to 1/2 of kettle radius, and still wall and stirring in rib is provided with the mobile cavity for superheated vapour of one.
6. according to the described intelligent trade waste reactor device systems of claim 3 to 5 any one, it is characterized in that:
The axial angle α span of described stirring rib and kettle rotating shaft is 20～30 °, and cross section the above stirring rib and the kettle angle β span in the radial direction axial perpendicular to rotating shaft at kettle are 5～15 °.
7. according to the described intelligent trade waste reactor device systems of claim 3 to 5 any one, it is characterized in that:
The tubbiness rotary body that described kettle is horizontal inclined placement is provided with in the heart material exchange mouthful in kettle inner cone lid, and material exchange mouth is provided with to reinforced feeding device in kettle, and feeding device is provided with loading hopper and the dump skip be connected with material exchange mouth;
Described kettle front and back ends is provided with the forward and backward carrier base that supports its rotation;
The kettle downside is provided with the power set that drive kettle to rotate.
8. according to the described intelligent trade waste reactor device systems of claim 3 or 4, it is characterized in that:
Described still wall is along circumferentially being divided into a plurality of heating intervals, the axial coil pipe formed after each heating interval inner heat-conductive pipe series connection is communicated with respectively with the swivel joint that the kettle rear end arranges, heat pipe in each heating interval is connected with the input flexible pipe of setting by swivel joint, and the heat pipe in each heating interval also is connected with the delivery hose of setting by swivel joint;
Be provided with the thermal source section that supplies with conduction oil to heat pipe at the kettle rear side, the output of thermal source section is connected with separator, the input of thermal source section is connected with oil catcher, all input flexible pipes are communicated with separator is in parallel, all delivery hoses and oil catcher are in parallel to be communicated with, the soft circulation circuit of described thermal source section, separator, input flexible pipe, swivel joint, heat pipe, delivery hose and a sealing of oil catcher formation.
9. intelligent trade waste reactor device systems according to claim 5, it is characterized in that: described still wall and the cavity stirred in rib are communicated with a swivel joint, this swivel joint is connected with the input flexible pipe, be provided with and supply with the thermal source section of superheated vapour by the input flexible pipe to still wall and the cavity in the stirring rib at the kettle rear side, also be provided with on kettle with still wall and the cavity stirred in rib and be communicated with the drain valve of being convenient to condensed water discharge in cavity.
10. intelligent trade waste reactor device systems according to claim 5, it is characterized in that, described power set comprise electromagnetic adjustable speed motor and reduction box, between electromagnetic adjustable speed motor and reduction box, by belt pulley, be connected, on the output shaft of reduction box, pinion is installed, corresponding upwards is provided with the gear wheel coordinated with pinion in kettle wall week.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013101087652A CN103433266A (en) | 2013-03-31 | 2013-03-31 | Intelligent reaction kettle equipment system for industrial wastes |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013101087652A CN103433266A (en) | 2013-03-31 | 2013-03-31 | Intelligent reaction kettle equipment system for industrial wastes |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103433266A true CN103433266A (en) | 2013-12-11 |
Family
ID=49687031
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013101087652A Pending CN103433266A (en) | 2013-03-31 | 2013-03-31 | Intelligent reaction kettle equipment system for industrial wastes |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103433266A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105183051A (en) * | 2015-09-28 | 2015-12-23 | 夏烬楚 | Automatic graphite evaporator control system and method |
| CN105204425A (en) * | 2015-09-28 | 2015-12-30 | 夏烬楚 | Method for automatically controlling graphite evaporator |
| CN105277007A (en) * | 2015-09-28 | 2016-01-27 | 夏烬楚 | Control system and method for novel graphite condenser |
| CN106371480A (en) * | 2015-07-24 | 2017-02-01 | 中船重工海博威（江苏）科技发展有限公司 | Electric heating temperature control system and method for ammonia-containing waste gas treatment through catalytic oxidation |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5190226A (en) * | 1991-04-29 | 1993-03-02 | Holloway Clifford C | Apparatus and method for separation, recovery, and recycling municipal solid waste and the like |
| JP2002028613A (en) * | 2000-07-19 | 2002-01-29 | Tokyokoki Seizosho Ltd | High temperature high pressure submerged oxidation decomposition device |
| CN101171084A (en) * | 2005-05-05 | 2008-04-30 | 埃斯泰克有限责任公司 | Waste processing apparatus and method |
| CN101448581A (en) * | 2006-09-28 | 2009-06-03 | Eco原料株式会社 | Processing system for organic waste |
| CN201399344Y (en) * | 2009-04-07 | 2010-02-10 | 朱伟荣 | Cracking kettle |
| CN202105611U (en) * | 2011-04-20 | 2012-01-11 | 江苏赛欧信越消泡剂有限公司 | Heating and mixing paddle of polymerization reactor |
| CN102794148A (en) * | 2012-07-19 | 2012-11-28 | 江苏中旗作物保护股份有限公司 | Automatically-controlled steam heating reaction kettle |
-
2013
- 2013-03-31 CN CN2013101087652A patent/CN103433266A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5190226A (en) * | 1991-04-29 | 1993-03-02 | Holloway Clifford C | Apparatus and method for separation, recovery, and recycling municipal solid waste and the like |
| JP2002028613A (en) * | 2000-07-19 | 2002-01-29 | Tokyokoki Seizosho Ltd | High temperature high pressure submerged oxidation decomposition device |
| CN101171084A (en) * | 2005-05-05 | 2008-04-30 | 埃斯泰克有限责任公司 | Waste processing apparatus and method |
| CN101448581A (en) * | 2006-09-28 | 2009-06-03 | Eco原料株式会社 | Processing system for organic waste |
| CN201399344Y (en) * | 2009-04-07 | 2010-02-10 | 朱伟荣 | Cracking kettle |
| CN202105611U (en) * | 2011-04-20 | 2012-01-11 | 江苏赛欧信越消泡剂有限公司 | Heating and mixing paddle of polymerization reactor |
| CN102794148A (en) * | 2012-07-19 | 2012-11-28 | 江苏中旗作物保护股份有限公司 | Automatically-controlled steam heating reaction kettle |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106371480A (en) * | 2015-07-24 | 2017-02-01 | 中船重工海博威（江苏）科技发展有限公司 | Electric heating temperature control system and method for ammonia-containing waste gas treatment through catalytic oxidation |
| CN106371480B (en) * | 2015-07-24 | 2018-09-04 | 中船重工海博威（江苏）科技发展有限公司 | A kind of catalytic oxidation treatment ammonia-contaminated gas electricity consumption heating and temperature control system and method |
| CN105183051A (en) * | 2015-09-28 | 2015-12-23 | 夏烬楚 | Automatic graphite evaporator control system and method |
| CN105204425A (en) * | 2015-09-28 | 2015-12-30 | 夏烬楚 | Method for automatically controlling graphite evaporator |
| CN105277007A (en) * | 2015-09-28 | 2016-01-27 | 夏烬楚 | Control system and method for novel graphite condenser |
| CN105183051B (en) * | 2015-09-28 | 2017-12-12 | 江苏锡沂高新区科技发展有限公司 | The automatic control system and method for a kind of graphite evaporator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101844859B (en) | Complete steam low-temperature thermally tempering and drying device and method for sludge | |
| CN101993181B (en) | Method for dehydration and recycling of continuous dyeing sludge | |
| CN104072212A (en) | Intelligent device for composting kitchen wastes | |
| CN105417923B (en) | A kind of sludge drying system | |
| CN103433266A (en) | Intelligent reaction kettle equipment system for industrial wastes | |
| CN103990643B (en) | A kind of damp and hot carbonization treatment method of biomass castoff low temperature and system | |
| CN103230770B (en) | Biological oxidation and high temperature pyrolysis reactor and input and output material control method thereof | |
| CN207845559U (en) | A kind of novel sludge carbonization device | |
| CN103964903A (en) | Anaerobic and aerobic fermentation coupling device for organic garbage treatment | |
| CN102311215A (en) | Urban life sludge locally self-circulation comprehensive utilization device and method | |
| CN103521131B (en) | Intelligent equipment system for preparing forestry and agricultural residue derived fuel by using forestry and agricultural residues | |
| CN211645009U (en) | Dirty comprehensive utilization system of excrement | |
| CN109082287A (en) | Applied microwave technology carries out the dry integrated apparatus with pyrolysis processing of feces of livestock and poultry | |
| CN206428136U (en) | Drum-type feces of livestock and poultry is dehydrated fermentor | |
| CN201753303U (en) | Steam low-temperature quenching and tempering complete sludge drying device | |
| CN104789467B (en) | A kind of food garbage Anaerobic Digestion device | |
| CN202519253U (en) | Circulating water system for aerobic fermentation reaction | |
| CN203855576U (en) | Renewable energy preparation system | |
| CN216080881U (en) | Forced drainage high-efficiency heating dryer | |
| CN104910936A (en) | Enhanced heat transfer-based biomass continuous pyrolysis device, and method | |
| CN201952369U (en) | Solar bio-treater for organic wastes | |
| CN104449791A (en) | Peristaltic solid-phase reactor and combined module | |
| CN204211688U (en) | One way of life rubbish multi-layer rotary destructive distillation device | |
| CN203999121U (en) | A kind of biochemical reactor of using capable of circulation | |
| CN210080332U (en) | Device for degrading kitchen waste by using microorganisms |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20131211 |