The utility model content
The purpose of this utility model is to provide a kind of active carbocoal filtering adsorption material processing equipment, to overcome the defective that known technology exists.
For achieving the above object, the active carbocoal filtering adsorption material processing equipment that the utility model provides includes:
One cylinder, one end connect and add feed bin, and the other end connects drawing mechanism;
This drum sleeve middle part is located in the heating clamber, and heating clamber two side and cylinder bottom are equipped with several gas-fired mouths;
One end of cylinder outer wall is provided with the driving cog wheel rim, and the cylinder two ends respectively have one to support rolling ring, and this cylinder of a driven by motor rotates in heating clamber;
Heating used fuel gas pipeline is the dual circuit system.
Described active carbocoal filtering adsorption material processing equipment, wherein, cylinder connects an end that adds feed bin and is connected with gas collecting apparatus, and this gas collecting apparatus connects the gas-fired mouth.
Described active carbocoal filtering adsorption material processing equipment, wherein, the two-end part that cylinder contacts with heating clamber is equipped with sealing device, and sealing device is palace formula or steam-type.
Described active carbocoal filtering adsorption material processing equipment, wherein, the cylinder two ends respectively are provided with doffer, and the doffer inwall is installed material rotating plate, and the doffer inwall directly contacts with material.
Described active carbocoal filtering adsorption material processing equipment, wherein, the cylinder two ends respectively are equipped with temperature measuring equipment.
Described active carbocoal filtering adsorption material processing equipment, wherein, the motor that cylinder drives the cylinder rotation is a variable-frequency motor, drum rotation speed is 0.5-1.5r/min.
Described active carbocoal filtering adsorption material processing equipment, wherein, the heating clamber liner is light weeight alumina brick and high aluminum fiber mixed structure, the heating clamber top is the poly-flat furred ceiling of light brick of high alumina; It between heating clamber side wall and the unit casing light heat insulation material.
Described active carbocoal filtering adsorption material processing equipment, wherein, the exhaust opening that the flue gas in the heating clamber is installed by the unit top is discharged; This exhaust opening outer cover is provided with the waste heat water jacket.
Described active carbocoal filtering adsorption material processing equipment wherein, is equipped with a plurality of temperature measuring equipments on the chamber walls both sides.
Described active carbocoal filtering adsorption material processing equipment, wherein, equipment electrically connects a switch board.
Active carbocoal filtering adsorption material processing equipment by the utility model provides can satisfy preparation technology and require different temperature when the operation of preparation active carbocoal filtering adsorption material.
The specific embodiment
The active carbocoal filtering adsorption material processing equipment that the utility model provides, feed bin, screw(-type) feeder, gas collecting apparatus, cylinder, support rolling ring, transmission gear ring, chamber walls, reductor, variable-frequency motor, heating clamber, exhaust opening, low-pressure gas burner, temperature measuring equipment, material rotating plate, drawing mechanism, doffer, steam input pipe, peep hole, charging temperature measuring equipment, discharging temperature measuring equipment, sealing device are formed by adding, combustion fan, dust arrester, waste heat water jacket, air-introduced machine, gas exhaust machine, unit casing etc. are formed.
The cylinder of the utility model equipment is made the material selection heat-resistance stainless steel, and the high temperature in the time of can bearing unit operation can be resisted general soda acid salt corrosion.Diameter of cylinder is 600mm~2,000mm, and length 18,000~28,000mm, cylinder is divided into following temperature section by temperature curve:
Section 1 heats up: 20 ℃~400 ℃ of running temperatures, 4 ℃~6 ℃/min of heating rate;
Section 2 heats up: 400 ℃~600 ℃ of running temperatures, 4 ℃~6 ℃/min of heating rate;
Constant temperature zone 1: 600 ℃ of running temperatures, constant temperature 40~60 minutes;
Section 3 heats up: 600 ℃~800 ℃ of running temperatures, 6 ℃~8 ℃/min of heating rate;
Activation section 2: 840 ℃~950 ℃ of running temperatures, the time of activation is 20~60 minutes;
Temperature descending section 1: 950 ℃~400 ℃ of running temperatures.
Sealing device is installed at the position that the cylinder two ends contact with heating clamber, and sealing device adopts labyrinth type or steam-type.The cylinder two ends are respectively with 1 meter long doffer, and inner wall of rotary drum is installed and dug a spoonful shape material rotating plate, and the material rotating plate material is identical with cylinder, and inner wall of rotary drum directly contacts with material, and upper and lower layer material alternately is heated homogeneous heating.Material is delivered to the burning of low-pressure gas burner at the heating gas of cylinder inner drying and the generation of destructive distillation stage after the gas collecting apparatus collection by drum front end.Material enters temperature descending section after going out activation section, and cooling naturally is until discharging.Cylinder respectively has 1 to support rolling ring by the front and back end, and cylinder outer wall is inlayed the driving cog wheel rim, is driven by reductor, variable-frequency motor.Cylinder design rotating speed 0.5~1.5r/min, variable-frequency stepless speed-regulating.The cylinder mounted angle is 2 °.At the unit middle part is heating clamber, by the external heat cylinder outer wall.The low-pressure gas burner is installed on the heating clamber two side, provides when burning required air by combustion fan, the low-pressure gas burner is positioned at the cylinder bottom, avoids the flame of low-pressure gas burner ejection directly to contact with cylinder.The low-pressure gas burner is established 10~16 altogether according to temperature curve, arranged crosswise on the heating clamber two side, temperature by each section in the air demand control heating clamber of regulating each low-pressure gas burner guarantees temperature, heating-up time and constant temperature time that active carbocoal filtering adsorption material preparation technology requires.It is that the heating gas that produces is decomposed in the dry distillation of coal in the heating gas that produces of gas generator and the unit running process that the utility model provides unit fuel, fuel gas pipeline designs according to the dual circuit system, adopt the gas generator heating gas during unit initial launch, temperature in unit reach a certain height, decompose after the dry distillation of coal in the unit and switch pipeline when producing heating gas, utilize the dry distillation of coal in the unit to decompose the heating gas burning heating that produces.
The chamber walls liner is light weeight alumina brick and high aluminum fiber mixed structure, and the heating clamber top is the poly-flat furred ceiling of light brick of high alumina, and convenient disassembly during the maintenance cylinder is a light heat insulation material between heating clamber side wall and the unit casing, and it is few to hold heat dissipation capacity, quick heating.Unit casing is shaped steel, steel plate structure.
The exhaust opening that flue gas in the unit heating clamber is installed by the unit top is discharged, and exhaust opening is connected with waste heat water jacket, air-introduced machine, and air-introduced machine adopts frequency control, and the remaining hot water cover is used for reclaiming heat, reduction flue-gas temperature, the heating steam boiler replenishing water of flue gas.
A plurality of temperature measuring equipments are installed on the chamber walls both sides, detect the temperature of each temperature section, at unit head, tail temperature measuring equipment is installed, detect feeding temperature and drop temperature, unit is established 1 switch board, 20 digital display meters, variable-frequency motor frequency converter and air-introduced machine frequency converter and screw(-type) feeder frequency converter and power switch and low-voltage electrical apparatus etc. are installed in the switch board.
The mists such as heating gas that material in the cylinder produces in process are collected by the drum front end gas collecting apparatus, and handle the back by gas exhaust machine through dust arrester, heating gas is delivered to unit low-pressure gas burner burn.Be provided with sealing device between gas collecting apparatus and the cylinder, sealing device can adopt labyrinth type, steam-type.
The front end of cylinder is equipped with screw(-type) feeder, adds feed bin, and the screw(-type) feeder charging rate is by the frequency-variable controller adjustment.The rear end of cylinder is equipped with drawing mechanism, and the end face of cylinder is provided with peep hole and steam access tube.Be provided with sealing device between drawing mechanism and the cylinder, sealing device can adopt labyrinth type, steam-type.
Active carbocoal filtering sorbing material described in the utility model is a raw material for adopting anthracite, meager coal, lean coal, coking coal, rich coal, bottle coal, jet coal, brown coal, semicoke, coke, basket charcoal, and drying, destructive distillation, carbonization, activation are prepared from, are used to handle the coal quality filtering sorbing material of industrial wastewater or municipal sewage.
Be further described below in conjunction with accompanying drawing:
High temperature when the cylinder 4 making material selection heat-resistance stainless steels of the utility model equipment can bear unit operation can be resisted general soda acid salt corrosion.Diameter of cylinder is 600mm~2,000mm, and length 18,000~28,000mm, cylinder 4 is divided into following temperature section by temperature curve:
Section 1 heats up: 20 ℃~400 ℃ of running temperatures, 4 ℃~6 ℃/min of heating rate;
Section 2 heats up: 400 ℃~600 ℃ of running temperatures, 4 ℃~6 ℃/min of heating rate;
Constant temperature zone 1: 600 ℃ of running temperatures, constant temperature 40~60 minutes;
Section 3 heats up: 600 ℃~800 ℃ of running temperatures, 6 ℃~8 ℃/min of heating rate;
Activation section 2: 840 ℃~950 ℃ of running temperatures, the time of activation is 20~60 minutes;
Temperature descending section 1: 950 ℃~400 ℃ of running temperatures.
Sealing device 21 is installed at the position that cylinder 4 two ends contact with heating clamber 10, and sealing device 21 adopts labyrinth type or steam-type.Cylinder 4 two ends are respectively with 1 meter long doffer 16, and cylinder 4 inwalls are installed and dug a spoonful shape material rotating plate 14, and material rotating plate 14 materials are identical with cylinder 4, and cylinder 4 inwalls directly contact with material, and upper and lower layer material can alternately be heated homogeneous heating.Material is delivered to low-pressure gas burner 12 at the heating gas of cylinder 4 inner dryings and the generation of destructive distillation stage after gas collecting apparatus 27 collections by cylinder 4 front ends.Material enters temperature descending section after going out activation section, and cooling naturally is until discharging.Cylinder 4 respectively has 1 to support rolling ring 5 by the front and back end, and cylinder 4 outer walls are inlayed transmission gear ring 6, is driven by reductor 8, variable-frequency motor 9.Cylinder 4 design speeds 0.5~1.5r/min, variable-frequency stepless speed-regulating.Cylinder 4 mounted angles are 2 °.
At the unit middle part is heating clamber 10, by the outer wall of external heat cylinder 4.Low-pressure gas burner 12 is installed on the both sides chamber walls 7, provides when burning required air by combustion fan 22, low-pressure gas burner 12 is positioned at cylinder 4 bottoms, avoids the flame of low-pressure gas burner 12 ejections directly to contact with cylinder 4.Low-pressure gas burner 12 is established 10~16 altogether according to temperature curve, arranged crosswise on both sides chamber walls 7, temperature by each section in the air demand control heating clamber 10 of regulating each low-pressure gas burner 12 guarantees temperature, heating-up time and constant temperature time that active carbocoal filtering adsorption material preparation technology requires.It is that the heating gas that produces is decomposed in the dry distillation of coal in the heating gas that produces of gas generator and the unit running process that the utility model provides unit fuel, fuel gas pipeline designs according to the dual circuit system, adopt the gas generator heating gas during unit initial launch, temperature in unit reach a certain height, decompose after the dry distillation of coal in the unit and switch pipeline when producing heating gas, utilize the dry distillation of coal in the unit to decompose the heating gas burning heating that produces.The liner of chamber walls 7 is light weeight alumina brick and high aluminum fiber mixed structure, and heating clamber 10 tops are the poly-flat furred ceiling of light brick of high alumina, and convenient disassembly during cylinder 4 maintenances is a light heat insulation material between chamber walls 7 and the unit casing 27, and it is few to hold heat dissipation capacity, quick heating.Unit casing 27 is shaped steel, steel plate structure.
The exhaust opening 11 that flue gas in the unit heating clamber 10 is installed by the unit top is discharged, exhaust opening 11 is equipped with waste heat water jacket 24, air-introduced machine 25, air-introduced machine 25 adopts frequency control, and waste heat water jacket 24 is used for reclaiming heat, reduction flue-gas temperature, the heating steam boiler replenishing water of flue gas.A plurality of temperature measuring equipments 13 are installed on the chamber walls 7, detect the temperature of each temperature section, at unit head, tail 1 temperature measuring equipment 13 is installed respectively, detect feeding temperature and drop temperature, unit is established 1 switch board, 20 digital display meters, variable-frequency motor 9 frequency converters and air-introduced machine 25 frequency converters and screw(-type) feeder 2 frequency converters and power switch and low-voltage electrical apparatus etc. are installed in the switch board.
The mists such as heating gas that materials in the cylinder 4 produce in process are collected by cylinder 4 front end gas collecting apparatus 3, and handle the back by gas exhaust machine 26 through dust arrester 23, heating gas is delivered to unit low-pressure gas burner 12 burn.Be provided with sealing device 21 between gas collecting apparatus 3 and the cylinder 4, sealing device 21 can adopt labyrinth type, steam-type.
The front end of cylinder 4 is equipped with screw(-type) feeder 2, adds feed bin 1, and screw(-type) feeder 2 charging rates are by the frequency-variable controller adjustment.The rear end of cylinder 4 is equipped with drawing mechanism 15, and the front end of cylinder 4 is provided with peep hole 18 and steam input pipe 17.Be provided with sealing device 21 between drawing mechanism 15 and cylinder 4 bodies, sealing device 21 can adopt labyrinth type, steam-type.
Active carbocoal filtering sorbing material described in the utility model is a raw material for adopting anthracite, meager coal, lean coal, coking coal, rich coal, bottle coal, jet coal, brown coal, semicoke, coke, basket charcoal, and drying, destructive distillation, carbonization, activation are prepared from, are used to handle the coal quality filtering sorbing material of industrial wastewater or municipal sewage.
Embodiment 1:
The cylinder 4 of the utility model equipment is made material selection heat-resistance stainless steel 310S (Cr25Ni20), and the high temperature in the time of can bearing unit operation can be resisted general soda acid salt corrosion.Cylinder 4 diameters are 2,000mm, and length 28,000mm, cylinder 4 is divided into following temperature section by temperature curve:
Section 1 heats up:
20 ℃~400 ℃ of running temperatures, 4 ℃~6 ℃/min of heating rate, this section drum length 8,000mm,
Section 2 heats up:
400 ℃~600 ℃ of running temperatures, 4 ℃~6 ℃/min of heating rate, this section drum length 4,000mm,
Constant temperature zone 1:
600 ℃ of running temperatures, constant temperature 40~60 minutes, this section drum length 3,000mm,
Section 3 heats up:
600 ℃~800 ℃ of running temperatures, 6 ℃~8 ℃/min of heating rate, this section drum length 3,000mm,
Activation section 2:
840 ℃~950 ℃ of running temperatures, soak time 20~60 minutes, this section drum length 5,000mm,
Temperature descending section 1:
950 ℃~400 ℃ of running temperatures, this section drum length 5,000mm,
Sealing device 21 is installed at the position that cylinder 4 two ends contact with heating clamber 10, and sealing device 21 adopts labyrinth type or steam-type.Cylinder 4 two ends are respectively with 1 meter long doffer 16, and cylinder 4 inwalls are installed and dug a spoonful shape material rotating plate 14, and material rotating plate 14 materials are identical with cylinder 4, and cylinder 4 inwalls directly contact with material, and upper and lower layer material alternately is heated homogeneous heating.Material is delivered to low-pressure gas burner 12 at the heating gas of cylinder 4 inner dryings and the generation of destructive distillation stage after gas collecting apparatus 3 collections by cylinder 4 front ends.Material enters temperature descending section after going out activation section, and cooling naturally is until discharging.
Cylinder 4 respectively has 1 to support rolling ring 5 by the front and back end, and cylinder 4 outer walls are inlayed transmission gear ring 6, is driven by reductor 8, variable-frequency motor 9.Cylinder 4 design speeds 0.5~1.5r/min, variable-frequency stepless speed-regulating.Cylinder 4 mounted angles are 2 °.
At the unit middle part is heating clamber 10, by the outer wall of external heat cylinder 4.Chamber walls 7 both sides are equipped with low-pressure gas burner 12, provide when burning required air by combustion fan 22, and low-pressure gas burner 12 is positioned at cylinder 4 bottoms, avoid the flame of low-pressure gas burner 12 ejections directly to contact with cylinder 4.Low-pressure gas burner 12 is established 10~16 altogether according to temperature curve, in chamber walls 7 both sides arranged crosswise, temperature by each section in the air demand control heating clamber 10 of regulating each low-pressure gas burner 12 guarantees temperature, heating-up time and constant temperature time that active carbocoal filtering adsorption material preparation technology requires.It is that the heating gas that produces is decomposed in the dry distillation of coal in the heating gas that produces of gas generator and the unit running process that the utility model provides unit fuel, fuel gas pipeline designs according to the dual circuit system, adopt the gas generator heating gas during unit initial launch, temperature in unit reach a certain height, decompose after the dry distillation of coal in the unit and switch pipeline when producing heating gas, utilize the dry distillation of coal in the unit to decompose the heating gas burning heating that produces.
The liner of chamber walls 7 is light weeight alumina brick and high aluminum fiber mixed structure, and heating clamber 10 tops are the poly-flat furred ceiling of light brick of high alumina, and convenient disassembly during cylinder 4 maintenances is a light heat insulation material between chamber walls 7 and the unit casing 27, and it is few to hold heat dissipation capacity, quick heating.Unit casing 27 is shaped steel, steel plate structure.
The exhaust opening 11 that flue gas in the unit heating clamber 10 is installed by the unit top is discharged, exhaust opening 11 is equipped with waste heat water jacket 24, air-introduced machine 25, air-introduced machine 25 adopts frequency control, and waste heat water jacket 24 is used for reclaiming heat, reduction flue-gas temperature, the heating steam boiler replenishing water of flue gas.
A plurality of temperature measuring equipments 13 are installed on the chamber walls 7; detect the temperature of each temperature section; at unit head, tail 1 temperature measuring equipment 13 is installed respectively; detect feeding temperature and drop temperature; temperature-detecting device is selected thermocouple for use; the using compensation lead is sent to instrument cabinet with thermocouple signal, adopts the metal hose shielding protection.Unit is established 1 switch board, and 20 digital display meters, variable-frequency motor 9 frequency converters and air-introduced machine 25 frequency converters and screw(-type) feeder 2 frequency converters and power switch and low-voltage electrical apparatus etc. are installed in the switch board.
The mists such as heating gas that materials in the cylinder 4 produce in process are collected by cylinder 4 front end gas collecting apparatus 3, and handle the back by gas exhaust machine 26 through dust arrester 23, heating gas is delivered to unit low-pressure gas burner 12 burn.Be provided with sealing device 21 between gas collecting apparatus 3 and the cylinder 4, sealing device 21 can adopt labyrinth type, steam-type.
The front end of cylinder 4 is equipped with screw(-type) feeder 2, adds feed bin 1, and screw(-type) feeder 2 charging rates are by the frequency-variable controller adjustment.The rear end of cylinder 4 is equipped with drawing mechanism 15, and the front end of cylinder 4 is provided with peep hole 18 and steam input pipe 17.Be provided with sealing device 21 between drawing mechanism 15 and cylinder 4 bodies, sealing device 21 can adopt labyrinth type, steam-type.
Active carbocoal filtering sorbing material described in the utility model is a raw material for adopting anthracite, meager coal, lean coal, coking coal, rich coal, bottle coal, jet coal, brown coal, semicoke, coke, basket charcoal, and drying, destructive distillation, carbonization, activation are prepared from, are used to handle the coal quality filtering sorbing material of industrial wastewater or municipal sewage.