CN203525725U - Regeneration equipment of active carbon - Google Patents
Regeneration equipment of active carbon Download PDFInfo
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- CN203525725U CN203525725U CN201320544811.9U CN201320544811U CN203525725U CN 203525725 U CN203525725 U CN 203525725U CN 201320544811 U CN201320544811 U CN 201320544811U CN 203525725 U CN203525725 U CN 203525725U
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- heating cabinet
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Abstract
The utility model discloses regeneration equipment of active carbon. The regeneration equipment comprises a desorption tower, wherein the desorption tower is a sealed tank body; the inner wall of the desorption tower is divided into five cavities by a first partition plate, a second partition plate, a third partition plate and a fourth partition plate; the five cavities are a material distribution region, a heating cabin, an exhaust region, a cooling cabin, and a discharge region; a heat exchange tube is arranged inside the heating cabin; the inner wall of the heating cabin is divided into a left heating cabin and a right heating cabin by a partition wall; the left heating cabin and the right heating cabin are the same in structure and are symmetrically arranged; a baffler plate is fixed inside the left heating cabin; a plurality of left air hoods are fixed on the outer wall of the left heating cabin; the left air hoods and the baffler plate are arranged at the same side; each left air hood is communicated with the inner wall of the left heating cabin; a baffle plate is respectively fixed at the position, corresponding to each left air hood, on the inner wall of the left heating cabin; the left heating cabin and the right heating cabin are respectively connected with a heat source. The regeneration equipment of the active carbon, which is disclosed by the utility model, can more thoroughly remove pollutants adsorbed by the active carbon, and is higher in efficiency.
Description
Technical field
The utility model relates to a kind of regenerating unit, relates to specifically the device that a kind of active carbon that makes absorption have pollutant is purified.
Background technology
In the sintering process of iron-smelter, in the flue gas discharging in the fossil fuel in thermal power plant or other compound combustion processes, contain oxysulfide, nitrogen oxide, heavy metal, bioxin, the pollution sources such as furans, remove these and pollute the mode that conventionally adopts charcoal absorption, active carbon after adsorption fouling thing, through the resolving in activated carbon regenerating equipment, in high temperature, the pollutant of absorption is resolved from active carbon, after separating, active carbon can be sent to adsorption tower cycling and reutilization, desorb and isolated pollutant are sent to other gas washing in SA production equipment or sulphur manufacturing equipment, produce sulfuric acid or sulphur for business., there is the problems such as efficiency is low, pollutant is removed not thoroughly, heat transfer efficiency is low in existing activated carbon regenerating equipment.
Utility model content
The purpose of this utility model is to provide a kind of reclaim equiment of active carbon, and it can remove the pollutant that active carbon adsorbs more up hill and dale, and efficiency is higher.
To achieve these goals, technical solution of the present utility model is: a kind of reclaim equiment of active carbon, comprise Analytic Tower, described Analytic Tower is closed tank, Analytic Tower inwall is by first, second, the 3rd, the 4th dividing plate is divided into disconnected five cavitys mutually, the product distribution region of these five cavitys for being arranged in order from top to bottom, heating cabinet, exhaust gas region, cooling storehouse, discharging region, top, product distribution region is provided with charging aperture, bottom, discharging region is provided with discharging opening, in heating cabinet, be provided with some heat hot exchanging tubes, the two ends of each heat hot exchanging tube are individually fixed in first, on second partition, and each heat hot exchanging tube upper end and product distribution regional connectivity, lower end is communicated with exhaust gas region, heating cabinet inwall is divided into a left side by partition wall, right heating cabinet, in left heating cabinet, be fixed with successively along its length several bafflers, each baffler is all positioned at the cross section of heating cabinet and the same side that each baffler is all fixed on left heating cabinet, between each baffler and left heating cabinet inwall, all leave spacing, left heating cabinet outer wall is fixed with several left airhoods, each left airhood is all positioned at the same side with baffler, each left airhood is all communicated with left heating cabinet inwall, the left heating cabinet inwall position corresponding with each left airhood middle part is fixed with respectively baffle plate, the cross section that baffle plate is positioned at left heating cabinet is divided into mutual disconnected two parts by left heating cabinet, the external and internal compositions of right heating cabinet is identical with the external and internal compositions of left heating cabinet, symmetrically, left, right heating cabinet is connected with respectively thermal source.
The reclaim equiment of the utility model active carbon, wherein, in described cooling storehouse, be provided with some heat of cooling exchanging tubes, the two ends of each heat of cooling exchanging tube are individually fixed in the 3rd, on the 4th dividing plate, and each heat of cooling exchanging tube upper end is communicated with exhaust gas region, lower end and discharging regional connectivity, cooling storehouse inwall is divided into a left side by partition wall, right cooling storehouse, wherein, in left cooling storehouse, be fixed with successively along its length several cooling storehouse bafflers, each cooling storehouse baffler is all positioned at the cross section in left cooling storehouse and the same side that each cooling storehouse baffler is all fixed on left cooling storehouse, between each cooling storehouse baffler and left cooling storehouse inwall, all leave spacing, left cooling storehouse outer wall is fixed with several left airhoods in cooling storehouse, each left airhood in cooling storehouse and cooling storehouse baffler are all positioned at the same side, each left airhood in cooling storehouse is all communicated with left cooling storehouse inwall, the inwall position corresponding with left airhood middle part, each cooling storehouse in left cooling storehouse is fixed with respectively cooling storehouse baffle plate, the cross section that cooling storehouse baffle plate is positioned at left cooling storehouse is divided into mutual disconnected two parts by cooling storehouse, a left side, the right external and internal compositions in cooling storehouse is identical with the external and internal compositions in left cooling storehouse, symmetrically, left, right cooling storehouse is connected with respectively low-temperature receiver.
The reclaim equiment of the utility model active carbon, wherein, described Analytic Tower upstream is provided with treating apparatus successively along the transmission direction of active carbon, dust arrester, top storage bin, feed arrangement, described feed arrangement is double helix dispenser, the discharging opening of this double helix dispenser is communicated with the charging aperture in described product distribution region, described Analytic Tower downstream is provided with discharge device successively along the transmission direction of active carbon, bottom storage bin, described discharge device is double helix dispenser, the feed end of this double helix dispenser is communicated with the discharging opening in discharging region, discharge end is communicated with bottom storage bin.
The reclaim equiment of the utility model active carbon, wherein, described product distribution region comprises raw material cabin and several distribution hoppers, and several distribution hoppers are arranged at raw material cabin below, and distribution hopper top is communicated with raw material cabin, bottom is communicated with the heat hot exchanging tube top in heating cabinet.
The reclaim equiment of the utility model active carbon, wherein, the double helix dispenser of described feed arrangement and the double helix dispenser of discharge device are all communicated with nitrogen, and described discharging region is communicated with nitrogen, and described product distribution regional connectivity has high temperature nitrogen.
The reclaim equiment of the utility model active carbon, wherein, described discharging region comprises buffer area, be arranged at several distribution hoppers of buffer area below and be positioned at the raw material cabin of distribution hopper below, each distribution hopper comprises hopper and is fixed on the transfer tube of hopper below, hopper is communicated with buffer area, and each transfer tube bottom is provided with switch, and this switch is controlled by cylinder, transfer tube bottom is communicated with raw material cabin by switch, and the discharging opening in discharging region is arranged at raw material cabin bottom.
The reclaim equiment of the utility model active carbon, wherein, described low-temperature receiver is air, cooling storehouse, a described left side is provided with cold air entry and exit, cold-air vent on left cooling storehouse is positioned at entrance top, cool air inlet on left cooling storehouse connects cold air air inlet pipe, cold air air inlet pipe is provided with filter, supply fan, air demand regulating fender, right cooling storehouse is provided with cold air entry and exit, cold-air vent on right cooling storehouse is positioned at entrance top, and the cool air inlet on right cooling storehouse is communicated with cold air air inlet pipe.
The reclaim equiment of the utility model active carbon, wherein, the cold-air vent in described left and right cooling storehouse is all connected on the blast pipe of cooling storehouse, and cooling storehouse blast pipe is communicated with atmosphere.
The reclaim equiment of the utility model active carbon, wherein, described thermal source is hot-air, described left heating cabinet is provided with hot-air and goes out, entrance, hot air outlet on left heating cabinet is positioned at entrance top, hot air inlet on described left heating cabinet is provided with heating cabinet air inlet pipe, heating cabinet air inlet pipe is communicated with air-source, and along airflow direction, be provided with successively supply fan in heating cabinet air inlet pipe, the first air demand regulating fender, heater, described cooling storehouse blast pipe is connected by intermediate duct with described heater, intermediate duct is provided with the second air demand regulating fender, described right heating cabinet is provided with hot-air and goes out, entrance, hot air outlet on right heating cabinet is positioned at entrance top, hot air inlet on right heating cabinet is communicated with described heating cabinet air inlet pipe, a described left side, the hot air outlet of right heating cabinet is all connected on heating cabinet blast pipe, heating cabinet blast pipe is provided with air flow sensor, air flow sensor, first, the second air demand regulating fender is all connected with control system.
The reclaim equiment of the utility model active carbon, wherein, in described heating cabinet air inlet pipe, in described heater downstream, be also provided with the first temperature sensor, described exhaust gas region is provided with the second temperature sensor, described heater is provided with fuel supply pipe road, fuel supply pipe road is provided with fuel duty regulating fender, and first, second temperature sensor and fuel duty regulating fender are all connected with described control system.
Adopt after such scheme, because the heating cabinet in the reclaim equiment Analytic Tower of the utility model active carbon is divided into left and right heating cabinet, in storehouse, be provided with heat hot exchanging tube, and be respectively equipped with baffler, baffle plate and airhood in left and right heating cabinet, therefore expanded heat exchange area, and thermal source tortuous rising in left and right heating cabinet, extend the holdup time, improve the intensification efficiency of heating cabinet, separating out of the polluter that promotion active carbon adsorbs, makes the pollutant in active carbon remove more thorough.
Because Analytic Tower upstream is provided with treating apparatus, feed arrangement, feed arrangement is double helix dispenser, Analytic Tower downstream is provided with discharge device, this discharge device is also double helix dispenser, therefore feeding and discharging can carry out continuously, whole reclaim equiment can continuous operation, guarantees steady air current in Analytic Tower, and raises the efficiency, product distribution region comprises raw material cabin and several distribution hoppers, by distribution hopper, makes active carbon uniform distribution enter each heat-exchange tube, between the double helix dispenser of feed arrangement and between the double helix dispenser of discharge device, be all communicated with nitrogen, discharging region is communicated with nitrogen, product distribution regional connectivity has high temperature nitrogen, therefore guarantee that in Analytic Tower, steady air current is not subject to ectocine, and in Analytic Tower, keep inert gas environment, fire-retardant, prevent because of high the causing danger too of temperature in Analytic Tower, and product distribution regional connectivity has high temperature nitrogen, prevent that low temperature nitrogen from entering in Analytic Tower, cause Analytic Tower internal condensation and cause corrosion, the nitrogen passing into can also promote the discharge of the gas that parses, raise the efficiency, cold and heat source all adopts air, makes to keep dry state in Analytic Tower, reduces corrosion, active carbon treated device before entering Analytic Tower sprays and has catalyst, and the catalyst on active carbon is intensified when active carbon heats up, and improves the adsorption capacity of active carbon.
Accompanying drawing explanation
Fig. 1 is the structural representation of the reclaim equiment of the utility model active carbon;
Fig. 2 is that the A-A of Fig. 1 is to cutaway view;
Fig. 3 is that the B-B of Fig. 1 is to cutaway view;
Fig. 4 is that the C-C of Fig. 1 is to cutaway view.
The specific embodiment
As shown in Figure 1, the reclaim equiment of the utility model active carbon comprises Analytic Tower 01, and Analytic Tower 01 is closed tank, and Analytic Tower 01 inwall is by first, second, the 3rd, the 4th dividing plate 11, 12, 13, 14 are divided into disconnected five cavitys mutually, the product distribution area 02 of these five cavitys for being arranged in order from top to bottom, heating cabinet 04, exhaust gas region 05, cooling storehouse 06, discharging region 07, product distribution area 02 tops are provided with charging aperture, and 07 bottom, discharging region is provided with discharging opening, is evenly equipped with many heat hot exchanging tubes 43 in heating cabinet 04, and the two ends of each heat hot exchanging tube 43 are welded in respectively first, second partition 11, on 12, and each heat hot exchanging tube 43 upper ends are communicated with product distribution area 02, lower end is communicated with exhaust gas region 05, and as shown in Figure 2, heating cabinet 04 inwall is divided into a mutual disconnected left side by partition wall 44, right heating cabinet 41, 42, the two ends up and down of partition wall 44 are welded in respectively first, second partition 11, on 12, in left heating cabinet 41, be welded with a plurality of bafflers 411, a plurality of bafflers 411 distribute successively along the length direction of left heating cabinet, each baffler is all positioned at the cross section of heating cabinet 04 and the left side that each baffler is all fixed on left heating cabinet 41, between each baffler and left heating cabinet inwall, all leave spacing 412, as shown in Figure 2, left heating cabinet 41 left side outer walls are fixed with two left airhoods 413, two left airhoods 413 are all communicated with left heating cabinet 41 inwalls, the left heating cabinet inwall position corresponding with two left airhood 413 middle parts is fixed with respectively baffle plate 414, the cross section that baffle plate 414 is positioned at left heating cabinet is divided into mutual disconnected two parts by left heating cabinet, the external and internal compositions of right heating cabinet 42 is identical with the external and internal compositions of left heating cabinet 41, symmetrically, a left side, right heating cabinet 41, 42 are connected with respectively thermal source.
Analytic Tower 01 upstream is provided with treating apparatus 31, dust arrester 32, top storage bin 33, feed arrangement 34 successively along the transmission direction of active carbon, feed arrangement 34 is double helix dispenser, the discharging opening of double helix dispenser is communicated with the charging aperture of described product distribution area 02, Analytic Tower 01 downstream is provided with discharge device 35, bottom storage bin 36 successively along the transmission direction of active carbon, discharge device 35 is double helix dispenser, and the feed end of this double helix dispenser is communicated with the discharging opening in discharging region 07, discharge end is communicated with bottom storage bin 36.
As Fig. 1,3 product distribution area 0s 2 comprise top raw material cabin 21 and several distribution hoppers 22, several distribution hoppers 22 are arranged at top raw material cabin 21 belows, distribution hopper 22 tops are communicated with raw material cabin 21, bottom is communicated with heat hot exchanging tube 43 tops in heating cabinet, and the discharging opening of the double helix dispenser of feed arrangement 34 is communicated with the charging aperture of top raw material cabin 21.
Exhaust gas region 05 is provided with exhaust outlet 51, and exhaust outlet 51 connects gas collector 53 by pipeline 52, and pipeline 52 is provided with scavenger fan and sensor.
In cooling storehouse 06, be provided with many heat of cooling exchanging tubes 63, the two ends of each heat of cooling exchanging tube 63 are individually fixed in the 3rd, the 4th dividing plate 13, on 14, and each heat of cooling exchanging tube 63 upper ends are communicated with exhaust gas region 05, lower end is communicated with discharging region 07, cooling storehouse 06 inwall is divided into a left side by partition wall, right cooling storehouse 61, 62, wherein, in left cooling storehouse 61, be fixed with successively along its length a plurality of cooling storehouses baffler 611, each cooling storehouse baffler is all positioned at the cross section in cooling storehouse 06 and the same side that each cooling storehouse baffler is all fixed on left cooling storehouse 61, between each cooling storehouse baffler and left cooling storehouse inwall, leave spacing 612, 61 outer wall left sides, left cooling storehouse are fixed with two left airhoods 613 in cooling storehouse, two left airhoods 613 in cooling storehouse are all communicated with left cooling storehouse 61 inwalls, the inwall position corresponding with left airhood 613 middle parts, two cooling storehouses, left cooling storehouse is fixed with respectively cooling storehouse baffle plate 614, the cross section that cooling storehouse baffle plate 614 is positioned at left cooling storehouse is divided into mutual disconnected two parts by cooling storehouse, a left side, the external and internal compositions in right cooling storehouse 62 is identical with the external and internal compositions in left cooling storehouse 61, symmetrically, left, right cooling storehouse 61, 62 are connected with respectively low-temperature receiver.
As shown in Fig. 1,4, discharging region 07 comprises buffer area 71, be arranged at a plurality of distribution hoppers 72 of buffer area 71 belows and be positioned at the raw material cabin 73 of distribution hopper 72 belows, each distribution hopper comprises hopper 721 and is fixed on the transfer tube 722 of hopper 721 belows, hopper 721 is communicated with buffer area 71, each transfer tube 722 bottoms are provided with switch, this switch is controlled by cylinder, and transfer tube 722 bottoms are communicated with raw material cabin 73 by switch, and discharging opening is arranged at raw material cabin 73 bottoms.
Source nitrogen 81 is communicated in respectively between the double helix dispenser of feed arrangement 34 by pipeline, between the double helix dispenser of discharge device 35, discharging region 07, product distribution area 02, the pipeline 811 that is communicated with product distribution area 02 is provided with heat exchanger 812, heat exchanger 812 is communicated with heating steam 813, and nitrogen passes into product distribution area 02 after Steam Heating.
Above-mentioned low-temperature receiver is air, left cooling storehouse 61 is provided with cold air entry and exit 616,617, outlet is positioned at entrance top, cool air inlet 617 connects cold air air inlet pipe 618, cold air air inlet pipe 618 is provided with filter, supply fan, air demand regulating fender, right cooling storehouse 62 is provided with cold air entry and exit 626,627, and outlet is positioned at entrance top, and this cool air inlet 627 is communicated with cold air air inlet pipe 618.
The cold-air vent 616,626 in left and right cooling storehouse 61,62 is all connected on cooling storehouse blast pipe 64, and cooling storehouse blast pipe 64 is communicated with atmosphere.
Above-mentioned thermal source is hot-air, left heating cabinet 41 is provided with hot-air and goes out, entrance 416, 417, outlet is positioned at entrance top, described hot air inlet 417 is provided with heating cabinet air inlet pipe 40, heating cabinet air inlet pipe 40 is communicated with air-source, and along airflow direction, be provided with successively supply fan 401 in heating cabinet air inlet pipe 40, the first air demand regulating fender 402, heater 403, cooling storehouse blast pipe 64 is connected by intermediate duct 641 with heater 403, intermediate duct 641 is provided with the second air demand regulating fender 642, right heating cabinet 42 is provided with hot-air and goes out, entrance 426, 427, outlet is positioned at entrance top, this hot air inlet is communicated with heating cabinet air inlet pipe 40, left, the hot air outlet of right heating cabinet is all connected on heating cabinet blast pipe 46, heating cabinet blast pipe 46 is provided with air flow sensor 461, air flow sensor 461, first, the second air demand regulating fender 402, 642 are all connected with control system.
In heating cabinet air inlet pipe 40, in heater 403 downstreams, be also provided with the first temperature sensor 404, exhaust gas region 05 is provided with the second temperature sensor 55, heater 403 is provided with fuel supply pipe road 405, fuel supply pipe road 405 is provided with fuel duty regulating fender 406, first, second temperature sensor 404,55 and fuel duty regulating fender 406 are all connected with above-mentioned control system, and heater 403 can fuel oil, combustion gas, fire coal or adopt electrical heating.
In adsorption tower, the pollution active carbon emitting by device for transferring, the transporting apparatus that is recycled system is transplanted on the reclaim equiment of the utility model active carbon, at the interior jet catalyst for the treatment of apparatus 31, after dust arrester 32 dedustings, the dust of activated carbon surface reduces, then enter top storage bin 33, under Action of Gravity Field, pollute active carbon and to the dual rotary dispenser of feed arrangement, drop into active carbon continuously from top storage bin 33, dual rotary dispenser is dual rotary valve structure, can transfer continuously large carbon content active, and continue to pass into nitrogen between upper and lower dispenser, when transferring active carbon continuously, cut off the gas flow in Analytic Tower, to keep sealing and inert condition.Enter the active carbon of Analytic Tower inside, be stored in top raw material cabin 21, in distribution hopper 22 drops to the heat hot exchanging tube 43 of heating cabinet 04, gas thermal source is through the hot air inlet 417 of left heating cabinet 41, the hot air inlet 427 of right heating cabinet 42 enters respectively a left side, in right heating cabinet 4, due to the baffler in heating cabinet, the effect of baffle plate and airhood, gas thermal source rises along path curve shown in Fig. 1, finally by hot air outlet 416, 426 discharge, expand heat exchange area, extend the holdup time of active carbon, improve the intensification efficiency of heating cabinet, active carbon in this process in heat hot exchanging tube 43 heats up gradually, conventionally be heated to 450 ℃, the catalyst being ejected on active carbon is intensified when active carbon heats up, improve the adsorption capacity of active carbon, and the pollution sources SO2 compound existing in waste gas and other adsorbent (as heavy metal Ji bioxin etc.), in this high-temperature region, start from active carbon, to resolve and separation, when active carbon is resolved, remain in the oxysulfide H in pore
2sO
4after being heated, in high temperature, be separated into SO
2, H
2o and CO
2, and from pore, parse oxysulfide (NH
4)
2sO
4when heating, be separated into NH
3, SO
3and H
2o parses ， bioxin from pore and also heating process, is decomposed into gas completely.Heat up, active carbon after parsing is discharged in exhaust gas region 05 in heat hot exchanging tube 43, at the interior above-mentioned gas parsing of exhaust gas region 05, through exhaust outlet 51, by pipeline 52, enter gas collector 53, further recycle, and under the effect of nitrogen, promote the discharge of gas, active carbon after exhaust enters in cooling storehouse 06, in cooling storehouse 06, low-temperature receiver gas is from a left side, right cooling storehouse 61, cool air inlet on 62 enters, along directivity curve shown in Fig. 1, rise and discharge by cold-air vent, partition wall in cooling storehouse, cooling storehouse baffle plate, cooling storehouse baffler, under the effect of cooling storehouse airhood, expand heat exchange area, extend the holdup time, improve the cooling efficiency in cooling storehouse, under the effect of gas low-temperature receiver, active carbon temperature in heat of cooling exchanging tube 63 enters discharging region 07 after reducing, active carbon is cooled to 20 ℃ of left and right conventionally.In discharging region 07, under the effect of cylinder, the switch opens of transfer tube 722 bottoms or close, when switch opens, it is temporary that active carbon in transfer tube 722 drops to lower feed storehouse 73 under Action of Gravity Field, through the dual rotary dispenser of discharge device, is expelled to bottom storage bin 36, continues input nitrogen between the dual rotary dispenser of discharge device, air in Analytic Tower is isolated from the outside, makes the interior steady air current of Analytic Tower and keep inert environments.Active carbon in the storage bin 36 of bottom can drop into adsorption tower and reuse, or comes into operation after the particle of removing small particle and dust state through vibratory sieve 37 again.After gas heater via 403 heating that cooling storehouse blast pipe 64 is discharged as thermal source, when the air flow sensor 461 on heating cabinet blast pipe shows air mass flow lower than setting value, by control system, open the first air demand regulating fender 402, sucking extraneous air is supplemented, when air flow sensor 461 shows air mass flow higher than setting value, open the unnecessary air of the second air demand regulating fender 642 discharge.When the second temperature sensor 55 shows delivery temperature lower than setting value, should improve the temperature of the heated air in the shown heating cabinet air inlet pipe 40 of the first temperature sensor 404, by control system, fuel duty regulating fender 406 is opened, strengthen fuel duty, when the second temperature sensor 55 shows delivery temperature higher than setting value, reduce fuel duty.
The above embodiment is described preferred embodiment of the present utility model; not scope of the present utility model is limited; do not departing under the prerequisite of the utility model design spirit; various distortion and improvement that the common engineers and technicians in this area make the technical solution of the utility model, all should fall in the definite protection domain of claims of the present utility model.
Claims (10)
1. the reclaim equiment of an active carbon, comprise Analytic Tower (01), it is characterized in that: described Analytic Tower (01) is closed tank, Analytic Tower (01) inwall is by first, second, the 3rd, the 4th dividing plate (11, 12, 13, 14) be divided into disconnected five cavitys mutually, the product distribution region (02) of these five cavitys for being arranged in order from top to bottom, heating cabinet (04), exhaust gas region (05), cooling storehouse (06), discharging region (07), top, product distribution region (02) is provided with charging aperture, bottom, discharging region (07) is provided with discharging opening, in heating cabinet (04), be provided with some heat hot exchanging tubes (43), the two ends of each heat hot exchanging tube (43) are individually fixed in first, second partition (11, 12) on, and each heat hot exchanging tube (43) upper end is communicated with product distribution region (02), lower end is communicated with exhaust gas region (05), heating cabinet (04) inwall is divided into a left side by partition wall (44), right heating cabinet (41, 42), in left heating cabinet (41), be fixed with successively along its length several bafflers (411), each baffler is all positioned at the cross section of heating cabinet (04) and the same side that each baffler is all fixed on left heating cabinet (41), between each baffler and left heating cabinet inwall, all leave spacing (412), left heating cabinet (41) outer wall is fixed with several left airhoods (413), each left airhood (413) is all positioned at the same side with baffler (411), each left airhood (413) is all communicated with left heating cabinet (41) inwall, the left heating cabinet inwall position corresponding with each left airhood (413) middle part is fixed with respectively baffle plate (414), the cross section that baffle plate (414) is positioned at left heating cabinet is divided into mutual disconnected two parts by left heating cabinet, the external and internal compositions of right heating cabinet (42) is identical with the external and internal compositions of left heating cabinet (41), symmetrically, left, right heating cabinet (41, 42) be connected with respectively thermal source.
2. the reclaim equiment of active carbon as claimed in claim 1, it is characterized in that: in described cooling storehouse (06), be provided with some heat of cooling exchanging tubes (63), the two ends of each heat of cooling exchanging tube (63) are individually fixed in the 3rd, the 4th dividing plate (13, 14) on, and each heat of cooling exchanging tube (63) upper end is communicated with exhaust gas region (05), lower end is communicated with discharging region (07), cooling storehouse (06) inwall is divided into a left side by partition wall, right cooling storehouse (61, 62), wherein, in left cooling storehouse (61), be fixed with successively along its length several cooling storehouse bafflers (611), each cooling storehouse baffler is all positioned at the cross section in left cooling storehouse (06) and the same side that each cooling storehouse baffler is all fixed on left cooling storehouse (61), between each cooling storehouse baffler and left cooling storehouse inwall, all leave spacing (612), left cooling storehouse (61) outer wall is fixed with the left airhoods in several cooling storehouses (613), each left airhood in cooling storehouse and cooling storehouse baffler are all positioned at the same side, the left airhood in each cooling storehouse (613) is all communicated with left cooling storehouse (61) inwall, the inwall position corresponding with the left airhood in each cooling storehouse (613) middle part in left cooling storehouse is fixed with respectively cooling storehouse baffle plate (614), the cross section that cooling storehouse baffle plate (614) is positioned at left cooling storehouse is divided into mutual disconnected two parts by cooling storehouse, a left side, the external and internal compositions in right cooling storehouse (62) is identical with the external and internal compositions in left cooling storehouse (61), symmetrically, left, right cooling storehouse (61, 62) be connected with respectively low-temperature receiver.
3. the reclaim equiment of active carbon as claimed in claim 2, it is characterized in that: described Analytic Tower (01) upstream is provided with treating apparatus (31) successively along the transmission direction of active carbon, dust arrester (32), top storage bin (33), feed arrangement (34), described feed arrangement (34) is double helix dispenser, the discharging opening of this double helix dispenser is communicated with the charging aperture in described product distribution region (02), described Analytic Tower (01) downstream is provided with discharge device (35) successively along the transmission direction of active carbon, bottom storage bin (36), described discharge device (35) is double helix dispenser, the feed end of this double helix dispenser is communicated with the discharging opening of discharging region (07), discharge end is communicated with bottom storage bin (36).
4. the reclaim equiment of active carbon as claimed in claim 3, it is characterized in that: described product distribution region (02) comprises raw material cabin (21) and several distribution hoppers (22), several distribution hoppers (22) are arranged at raw material cabin (21) below, and distribution hopper (22) top is communicated with raw material cabin (21), bottom is communicated with heat hot exchanging tube (43) top in heating cabinet.
5. the reclaim equiment of active carbon as claimed in claim 4, it is characterized in that: the double helix dispenser of the double helix dispenser of described feed arrangement (34) and discharge device (35) is all communicated with nitrogen, described discharging region (07) is communicated with nitrogen, and described product distribution region (02) is communicated with high temperature nitrogen.
6. the reclaim equiment of active carbon as claimed in claim 5, it is characterized in that: described discharging region (07) comprises buffer area (71), be arranged at several distribution hoppers (72) of buffer area (71) below and be positioned at the raw material cabin (73) of distribution hopper (72) below, each distribution hopper comprises hopper (721) and is fixed on the transfer tube (722) of hopper (721) below, hopper (721) is communicated with buffer area (71), each transfer tube (722) bottom is provided with switch, this switch is controlled by cylinder, transfer tube (722) bottom is communicated with raw material cabin (73) by switch, the discharging opening in discharging region (07) is arranged at raw material cabin (73) bottom.
7. the reclaim equiment of active carbon as claimed in claim 6, it is characterized in that: described low-temperature receiver is air, cooling storehouse, a described left side (61) is provided with cold air and goes out, entrance (616, 617), cold-air vent on left cooling storehouse (61) is positioned at entrance top, cool air inlet (617) on left cooling storehouse (61) connects cold air air inlet pipe (618), cold air air inlet pipe (618) is provided with filter, supply fan, air demand regulating fender, right cooling storehouse (62) is provided with cold air and goes out, entrance (626, 627), cold-air vent on right cooling storehouse (62) is positioned at entrance top, cool air inlet (627) on right cooling storehouse (62) is communicated with cold air air inlet pipe (618).
8. the reclaim equiment of active carbon as claimed in claim 7, is characterized in that: it is upper that the cold-air vent (616,626) in described left and right cooling storehouse (61,62) is all connected in cooling storehouse blast pipe (64), and cooling storehouse blast pipe (64) is communicated with atmosphere.
9. the reclaim equiment of active carbon as claimed in claim 8, it is characterized in that: described thermal source is hot-air, described left heating cabinet (41) is provided with hot-air and goes out, entrance (416, 417), hot air outlet on left heating cabinet is positioned at entrance top, hot air inlet (417) on described left heating cabinet is provided with heating cabinet air inlet pipe (40), heating cabinet air inlet pipe (40) is communicated with air-source, and heating cabinet air inlet pipe (40) is upper is provided with supply fan (401) successively along airflow direction, the first air demand regulating fender (402), heater (403), described cooling storehouse blast pipe (64) is connected by intermediate duct (641) with described heater (403), intermediate duct (641) is provided with the second air demand regulating fender (642), described right heating cabinet (42) is provided with hot-air and goes out, entrance (426, 427), hot air outlet on right heating cabinet (42) is positioned at entrance top, hot air inlet on right heating cabinet is communicated with described heating cabinet air inlet pipe (40), a described left side, the hot air outlet of right heating cabinet is all connected on heating cabinet blast pipe (46), heating cabinet blast pipe (46) is provided with air flow sensor (461), air flow sensor (461), first, the second air demand regulating fender (402, 642) be all connected with control system.
10. the reclaim equiment of active carbon as claimed in claim 9, it is characterized in that: described heating cabinet air inlet pipe (40) is upper is also provided with the first temperature sensor (404) in described heater (403) downstream, described exhaust gas region (05) is provided with the second temperature sensor (55), described heater (403) is provided with fuel supply pipe road (405), fuel supply pipe road (405) is provided with fuel duty regulating fender (406), and first, second temperature sensor (404,55) and fuel duty regulating fender (406) are all connected with described control system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320544811.9U CN203525725U (en) | 2013-09-03 | 2013-09-03 | Regeneration equipment of active carbon |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320544811.9U CN203525725U (en) | 2013-09-03 | 2013-09-03 | Regeneration equipment of active carbon |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103521200A (en) * | 2013-09-03 | 2014-01-22 | 香港诺曼泰壹环保科技有限公司 | Activated carbon regeneration equipment |
| CN107335476A (en) * | 2017-08-15 | 2017-11-10 | 国电科学技术研究院 | A kind of regenerator continuous-feeding air-lock device |
-
2013
- 2013-09-03 CN CN201320544811.9U patent/CN203525725U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103521200A (en) * | 2013-09-03 | 2014-01-22 | 香港诺曼泰壹环保科技有限公司 | Activated carbon regeneration equipment |
| CN103521200B (en) * | 2013-09-03 | 2015-08-12 | 香港诺曼泰壹环保科技有限公司 | The reclaim equiment of active carbon |
| CN107335476A (en) * | 2017-08-15 | 2017-11-10 | 国电科学技术研究院 | A kind of regenerator continuous-feeding air-lock device |
| CN107335476B (en) * | 2017-08-15 | 2024-01-16 | 国家能源集团科学技术研究院有限公司 | Continuous feeding and air locking device for regeneration tower |
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