CN205505017U - High concentration contains fluoride and chloride pharmaceutical factory residue integrated treatment recovery unit - Google Patents
High concentration contains fluoride and chloride pharmaceutical factory residue integrated treatment recovery unit Download PDFInfo
- Publication number
- CN205505017U CN205505017U CN201620042000.2U CN201620042000U CN205505017U CN 205505017 U CN205505017 U CN 205505017U CN 201620042000 U CN201620042000 U CN 201620042000U CN 205505017 U CN205505017 U CN 205505017U
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- rotary kiln
- integrated treatment
- pharmaceutical factory
- retracting device
- kiln
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- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 title claims abstract description 7
- 238000011084 recovery Methods 0.000 title abstract description 4
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 title abstract 2
- 238000000197 pyrolysis Methods 0.000 claims abstract description 16
- 238000001179 sorption measurement Methods 0.000 claims abstract description 4
- 238000001354 calcination Methods 0.000 claims description 16
- 239000002893 slag Substances 0.000 claims description 15
- 238000010304 firing Methods 0.000 claims description 13
- 230000009977 dual effect Effects 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 9
- 238000005453 pelletization Methods 0.000 claims description 8
- 238000005507 spraying Methods 0.000 claims description 8
- 238000005979 thermal decomposition reaction Methods 0.000 claims description 8
- 239000002918 waste heat Substances 0.000 claims description 8
- 150000001875 compounds Chemical class 0.000 claims description 4
- 239000003463 adsorbent Substances 0.000 claims description 3
- 239000002250 absorbent Substances 0.000 claims 1
- 230000002745 absorbent Effects 0.000 claims 1
- 239000003610 charcoal Substances 0.000 claims 1
- 239000003546 flue gas Substances 0.000 abstract description 24
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 23
- 239000007789 gas Substances 0.000 abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 7
- 238000002309 gasification Methods 0.000 abstract description 6
- 238000002485 combustion reaction Methods 0.000 abstract description 4
- 239000000428 dust Substances 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 abstract description 2
- 238000010521 absorption reaction Methods 0.000 abstract 1
- 229910052799 carbon Inorganic materials 0.000 abstract 1
- 238000009776 industrial production Methods 0.000 abstract 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 12
- 238000003889 chemical engineering Methods 0.000 description 9
- 239000010802 sludge Substances 0.000 description 9
- 239000000126 substance Substances 0.000 description 9
- 239000002699 waste material Substances 0.000 description 9
- 239000000463 material Substances 0.000 description 8
- 239000012141 concentrate Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 4
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 4
- 239000001110 calcium chloride Substances 0.000 description 4
- 229910001628 calcium chloride Inorganic materials 0.000 description 4
- 235000011148 calcium chloride Nutrition 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000011068 loading method Methods 0.000 description 4
- 229910019142 PO4 Inorganic materials 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 231100000862 numbness Toxicity 0.000 description 3
- 239000010452 phosphate Substances 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- PDDVQDOPXOGFQL-UHFFFAOYSA-N ClC1=NC=CC=C1.[F] Chemical compound ClC1=NC=CC=C1.[F] PDDVQDOPXOGFQL-UHFFFAOYSA-N 0.000 description 2
- 241001597008 Nomeidae Species 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000001925 catabolic effect Effects 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000012847 fine chemical Substances 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 208000027418 Wounds and injury Diseases 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007405 data analysis Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 229910052736 halogen Inorganic materials 0.000 description 1
- 150000002367 halogens Chemical class 0.000 description 1
- 125000000623 heterocyclic group Chemical group 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Landscapes
- Gasification And Melting Of Waste (AREA)
- Incineration Of Waste (AREA)
Abstract
The utility model relates to a high concentration contains fluoride and chloride pharmaceutical factory residue integrated treatment recovery unit, press flue gas flow, the device includes pyrolysis gasification incineration furnace, the one -level rotary kiln, the second grade rotary kiln, second combustion chamber, rapid cooling exhaust -heat boiler, the deacidification tower, the dust remover, the adsorption system, fan and chimney, characterized by adopts the flue with pyrolysis gasification incineration furnace, the one -level rotary kiln, the second grade rotary kiln, second combustion chamber, the deacidification tower, the dust remover, adsorption equipment, fan and chimney concatenate the intercommunication in proper order, pyrolysis gasification incineration furnace bottom is equipped with rotatory grate, one -level rotary kiln and second grade rotary kiln bottom are equipped with the slagging -off machine respectively. This system implementation innoxious and the resourceization of the dangerous discarded object of industrial production. The gas that produces in pyrolysis oven and the rotary kiln burns through second combustion chamber's high temperature and changes harmless gas into, handles through exhaust -heat boiler, deacidification tower, sack cleaner, active carbon absorption device to reach emission standard totally.
Description
Technical field
This utility model relates to the device that a kind of commercial production danger wastes joint disposal recycle device, the danger wastes harmlessness disposing particularly produced in fine-chemical intermediate production process and resource recycle.
Background technology
China is the whole world the first big pesticide medicine and intermediate manufacturing country, and yield wide in variety is big.Production process uses Technology of Fine Chemical Industry in a large number, such as the production of fluorine chloropyridine, produces the danger wastes such as substantial amounts of bottoms, saliferous concentrating spent liquor, saliferous chemical engineering sludge.These danger wastes i.e. contain fluorine chloropyridine and derivant, phenyl ring and derivant, halogenated hydrocarbons and various heterocycle Organic substance, also contains the inorganic matter such as calcium chloride, phosphate, also have the moisture content that cannot separate in a large number simultaneously.If animals and plants can be caused injury greatly by the most treated being flowed in natural environment, cause the death of crops and trees, the pernicious environmental accident such as person poultry poisoning.If not disposing stacking, long-term after these materials stack the most nowhere, storage barrel cage of long duration also can rupture leakage, exists and big environment hidden danger, and harm is permanent.
The present invention is directed to this type of present situation, contrast incineration disposal device at all kinds of dangerous waste, the minimizing of such danger wastes, innoxious, resource aspect have been carried out substantial amounts of research.Carry out fully comparing to the investment of device, energy consumption, efficiency, operating cost, disposal effect, it is proposed that integration series connection incineration disposal device, it is achieved that danger wastes decrement, toxic organic compound thoroughly burns, salt efficient recovery resource.
Utility model content
The purpose of this utility model is to provide a kind of collection " vertical continuous pyrolysis incinerator ", " one-level rotary kiln ", " two-stage rotary kiln ", " dual firing chamber " series winding one, it is possible not only to incinerating solid danger wastes simultaneously, and saliferous concentrated solution and chemical engineering sludge can be dried roasting harmless resource utilization, the incineration disposal device that treatment effeciency is high, overcomes the deficiency of existing single incinerator technology.
This utility model is achieved in that
A kind of high-concentration fluorine-contained compound and chloride pharmaceutical factory residue integrated treatment retracting device, including incinerator for thermal decomposition, one-level rotary kiln, two-stage rotary kiln, dual firing chamber, chilling waste heat boiler, extracting tower, cleaner unit, adsorption system, blower fan and chimney, it is characterized in that using flue that incinerator for thermal decomposition, one-level rotary kiln, two-stage rotary kiln, dual firing chamber, extracting tower, cleaner unit, adsorbent equipment, blower fan and chimney carry out concatenation connection successively, it is provided with rotary fire grate, one-level rotary kiln and two-stage rotary kiln bottom portion bottom incinerator for thermal decomposition and is respectively equipped with slag remover.
Described incinerator for thermal decomposition is vertical continuous pyrolysis incinerator, and the rotary fire grate arranged bottom it is tower grate formula rotary fire grate deslagging device.
Described one-level rotary kiln is that liquid slurry-spraying pelletizing turns round calcining kiln, and the slag remover arranged bottom it is dry slag-removing machine.
Described two-stage rotary kiln is that mud turns round calcining kiln, and the slag remover arranged bottom it is dry slag-removing machine.
Chilling waste heat boiler it is provided with between described dual firing chamber and extracting tower.
Described cleaner unit is sack cleaner.
Described extracting tower is half dry type extracting tower.
To achieve these goals, this utility model includes " vertical continuous pyrolysis incinerator " " saliferous concentrates residual liquid slurry-spraying pelletizing revolution calcining kiln (one-level rotary kiln) ", " saliferous chemical engineering sludge revolution calcining kiln (two-stage rotary kiln) ", dual firing chamber, chilling waste heat boiler, half dry type extracting tower, sack cleaner, activated carbon systems, blower fan and chimney.It is characterized in using flue " vertical continuous pyrolysis incinerator ", " one-level rotary kiln ", " two-stage rotary kiln ", " dual firing chamber " to be contacted.The high-temperature flue gas produced with " vertical continuous pyrolysis incinerator " is as " saliferous concentrates residual liquid slurry-spraying pelletizing revolution calcining kiln (one-level rotary kiln) ", the thermal source of " saliferous chemical engineering sludge revolution calcining kiln (two-stage rotary kiln) "; to wherein Organic substance dry distilling out, obtain containing few organic inorganic salts.According to the difference of the useless saliferous kind of danger, by difference dry distilling respectively in a two-stage rotary kiln of the useless mobility of dry distilling danger, it is separately recovered resource.One-level rotary kiln obtains calcium chloride, and two grades are returned loading of kiln and obtain phosphate.The high-temperature flue gas using " vertical continuous pyrolysis incinerator " to produce has following advantage as thermal source: (1) calorific value is high, and heat is big, but temperature is more applicable, and the inorganic salt being not result in back in loading of kiln melts.(2) incinerator flue gas oxygen content out is extremely low, entering into one or two grades, return will not be with carbonization gas exothermic heat of reaction in kiln in loading of kiln, it is easy to the control of kiln temperature, it is to avoid in kiln, inorganic salt melts.(3) by avoiding inorganic salt to melt measure, the useless thorough dry distilling of danger in kiln can be made, obtain high-purity inorganic salt.
" saliferous concentrates residual liquid slurry-spraying pelletizing revolution calcining kiln (one-level rotary kiln) " of the present utility model, " saliferous chemical engineering sludge revolution calcining kiln (two-stage rotary kiln) " all use dry-type slag discharger; have slag tap effective; waste heat recovery; the effect of energy-saving and water-saving, decreases substantial amounts of technological process and water treatment procedure than grain slag deslagging device.Mucking machine out inorganic salt can directly recycle.
Pyrolysis oven and time loading of kiln flue gas out enter dual firing chamber's oxygen-enriched combusting again, and holdup time >=2S, Organic substance and chloride are completely decomposed into the inorganic molecules materials such as water, carbon dioxide, HCl, HF, Cl2, SO2 by ignition temperature >=1100 DEG C.
Employing waste heat boiler cooling mode of the present utility model, be cooled to≤less than 250 DEG C by two combustion high-temperature flue gas (temperature >=1100 DEG C) out in 1s, it is to avoid the generation again of dioxin.The high-temperature steam that boiler produces can be used for productive life as heat source and power steam, accomplishes twice laid.
This utility model half dry type extracting tower, with NaOH solution and calcium oxide by acid gas removals such as the halogen in flue gas, sulfur, phosphorus, forms inorganic salt, makes acid gas emissions meet " dangerous waste incineration pollutant catabolic gene standard ".
This utility model uses the inorganic salt in 2 cleaner unit removing flue gases of the using and the reserved after dust, deacidification, makes discharge≤10mg/nm3, the highest.
This utility model uses activated carbon device again to remove Organic substance and the dioxin that flue gas middle reaches separate out, and makes dioxin reach extremely low level, reaches≤the EU criteria of 0.1ng-TEQ/Nm3.
Flue gas after process is used air-introduced machine and chimney to carry out high altitude discharge by this utility model device.Discharge meets " dangerous waste incineration pollutant catabolic gene standard ".
Accompanying drawing explanation
Fig. 1 is high-concentration fluorine-contained compound and chloride pharmaceutical factory residue integrated treatment retracting device structural representation.
In figure: 1-grab bucket, 2-vertical continuous pyrolysis incinerator, 3-tower numbness formula rotary fire grate deslagging device, 4-saliferous concentrate residual liquid slurry-spraying pelletizing revolution calcining kiln (one-level rotary kiln), 5-saliferous chemical engineering sludge revolution calcining kiln (two-stage rotary kiln), 6-dry-type slag discharger (1), 7-6-dry-type slag discharger (2), 8-dual firing chamber, 9-waste heat boiler, 10-deacidify tower, 11-sack cleaner (1) (2), 12-activated-carbon device, 13-air-introduced machine, 14-chimney.
Detailed description of the invention
In order to technical characteristic of the present utility model, purpose and effect are more clearly understood from; in conjunction with case study on implementation; a kind of three-phase mixed fluidized bed desulfurizer is further detailed, is not determinate, does not limits the protection domain of this utility patent with following case study on implementation.
Embodiment 1
Below in conjunction with the accompanying drawings this utility model is described in further detail.
This utility model automatic control system selects large centralised control system (SIEMENS PLC), arranges host computer man machine interface.The technological parameters such as the air capacity in pyrolytic gasification process and retort process, exhaust gas volumn, discharge, temperature, oxygen content, pressure, material input amount, fume emission and real time data are carried out collection in worksite, transmit, analyze, judgement processes, all devices and instrument to whole device are adjusted according to this.This control system have data acquisition, transmit, store, analyze judgement, equipment fault remotely diagnoses, report form statistics, graphic data analysis function.All data and operation can achieve in host computer industrial computer, and arrange data signal output interface, with local environment monitoring IDNet Inter Departmental Net, meet the requirement of supervision department.
Vertical continuous pyrolysis incinerator includes enclosed negative pressure material pit, driving grab bucket, the big hopper of import, closed double roller crushing feeder, body of heater, tower numbness formula gyratory crusher, primary air fan, combustor, sealing structure for water, mucking machine.Danger wastes carries out compatibility uniformly at negative pressure material pit, then is sent into the big hopper of import by driving grab bucket, by closed double roller crushing feeder feeding stove.In material entrance stove, after anoxycausis gasification, remaining lime-ash is crushed by tower numbness formula gyratory crusher, and mucking machine is discharged.
One-level rotary kiln is in tilted layout, and charging aperture is arranged at low level, downflow type flue gas at a high position, slag notch.Vertical continuous pyrolysis incinerator high-temperature flue gas out enters " saliferous concentrates residual liquid slurry-spraying pelletizing revolution calcining kiln (one-level rotary kiln) "; saliferous is concentrated residual liquid and sprays into from rotary kiln entrance by high-pressure spray gun; under the effect of high-temperature flue gas, the Organic substance of moisture and low-volatile starts to flash to gas, inorganic salt and high volatile organic compounds and mixes and separate on rotary kiln.Inorganic salt in rotary kiln and Organic substance constantly roll with rotary kiln thermally equivalent, slowly mobile to outlet, make material fully be heated and decompose, obtain high-purity inorganic salt (CaCl2).The inclination angle of rotary kiln is set according to Organic substance dry distilling resolving time, the form of material.High-purity inorganic salt (CaCl2) is got rid of with dry-type slag extractor.
Two-stage rotary kiln is in tilted layout, and charging aperture is in a high position, and slag notch is at low level, and reverse-flow flue gas is arranged.One-level rotary kiln flue gas out enters " saliferous chemical engineering sludge revolution calcining kiln (two-stage rotary kiln) " from low level, saliferous chemical engineering sludge uses cage feeding machine to send into a high position for rotary kiln, first moisture is evaporated with the low-temperature flue gas of rotary kiln outlet, with the high-temperature flue gas of rotary kiln entrance, the Organic substance in mud is thoroughly being decomposed, obtain inorganic salt (phosphate), then discharge with dry-type slag extractor.
Two-stage rotary kiln flue gas out is mixed with gasification flue gas and " saliferous concentrates residual liquid slurry-spraying pelletizing revolution calcining kiln (one-level rotary kiln) " and " saliferous chemical engineering sludge revolution calcining kiln (two-stage rotary kiln) " the dry distilling flue gas of " vertical continuous pyrolysis incinerator "; oxygen content and low in flue gas, calorific value is high.This mixed flue gas enters in dual firing chamber, sends into the oxygen-enriched abundant burning of sufficient secondary wind, ignition temperature >=1100 DEG C, gas residence time >=2s, makes the dioxin poisonous and harmful substance in flue gas thoroughly be decomposed in high temperature.After flue gas goes out dual firing chamber, after the multiple tracks purified treatment such as follow-up chilling, deacidification, dehydration, dedusting are up to standard, enter air.
In this explanation, narration partial content the most in detail belongs to industry universal knowledge, and professional and technical personnel in the field the most fully grasp.
The foregoing is only the schematic detailed description of the invention of this utility model, be not limited to scope of the present utility model.Any those skilled in the art, the equivalent variations made on the premise of without departing from design of the present utility model and principle and amendment, the scope of this utility model protection all should be belonged to.
Claims (8)
- The most high-concentration fluorine-contained compound and chloride pharmaceutical factory residue integrated treatment retracting device, including incinerator for thermal decomposition, one-level rotary kiln, two-stage rotary kiln, dual firing chamber, chilling waste heat boiler, extracting tower, cleaner unit, adsorption system, blower fan and chimney, it is characterized in that using flue that incinerator for thermal decomposition, one-level rotary kiln, two-stage rotary kiln, dual firing chamber, extracting tower, cleaner unit, adsorbent equipment, blower fan and chimney carry out concatenation connection successively, it is provided with rotary fire grate, one-level rotary kiln and two-stage rotary kiln bottom portion bottom incinerator for thermal decomposition and is respectively equipped with slag remover.
- 2. residue integrated treatment retracting device in pharmaceutical factory described in claim 1, is characterized in that described incinerator for thermal decomposition is vertical continuous pyrolysis incinerator, and the rotary fire grate arranged bottom it is tower grate formula rotary fire grate deslagging device.
- 3. residue integrated treatment retracting device in pharmaceutical factory described in claim 1, is characterized in that described one-level rotary kiln is that liquid slurry-spraying pelletizing turns round calcining kiln, and the slag remover arranged bottom it is dry slag-removing machine.
- 4. residue integrated treatment retracting device in pharmaceutical factory described in claim 1, is characterized in that described two-stage rotary kiln is that mud turns round calcining kiln, and the slag remover arranged bottom it is dry slag-removing machine.
- 5. residue integrated treatment retracting device in pharmaceutical factory described in claim 1, is characterized in that being provided with between described dual firing chamber and extracting tower chilling waste heat boiler.
- 6. residue integrated treatment retracting device in pharmaceutical factory described in claim 5, is characterized in that described cleaner unit is sack cleaner.
- 7. residue integrated treatment retracting device in pharmaceutical factory described in claim 5, is characterized in that described adsorbent equipment is absorbent charcoal adsorber.
- 8. residue integrated treatment retracting device in pharmaceutical factory described in claim 5, is characterized in that described extracting tower is half dry type extracting tower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620042000.2U CN205505017U (en) | 2016-01-18 | 2016-01-18 | High concentration contains fluoride and chloride pharmaceutical factory residue integrated treatment recovery unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620042000.2U CN205505017U (en) | 2016-01-18 | 2016-01-18 | High concentration contains fluoride and chloride pharmaceutical factory residue integrated treatment recovery unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205505017U true CN205505017U (en) | 2016-08-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620042000.2U Expired - Fee Related CN205505017U (en) | 2016-01-18 | 2016-01-18 | High concentration contains fluoride and chloride pharmaceutical factory residue integrated treatment recovery unit |
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| Country | Link |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106122983A (en) * | 2016-07-01 | 2016-11-16 | 无锡雪浪环境科技股份有限公司 | A kind of incinerator smoke is taken air-flow and is removed the devices and methods therefor of two English |
| CN108443889A (en) * | 2018-02-28 | 2018-08-24 | 上海锅炉厂有限公司 | A kind of discarded metal catalyst and organic sludge coprocessing device and method |
| CN108826319A (en) * | 2018-08-16 | 2018-11-16 | 东华工程科技股份有限公司 | Dangerous waste incinerator with dry colling slagging mechanism |
| CN114135875A (en) * | 2021-11-29 | 2022-03-04 | 广州雅居乐固体废物处理有限公司 | Incineration pretreatment process for high-fluorine solid waste |
| CN115028329A (en) * | 2022-07-11 | 2022-09-09 | 沈阳理工大学 | Comprehensive utilization method and system for thermal catalytic decomposition, separation and drying of sludge flue gas |
-
2016
- 2016-01-18 CN CN201620042000.2U patent/CN205505017U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106122983A (en) * | 2016-07-01 | 2016-11-16 | 无锡雪浪环境科技股份有限公司 | A kind of incinerator smoke is taken air-flow and is removed the devices and methods therefor of two English |
| CN106122983B (en) * | 2016-07-01 | 2018-07-20 | 无锡雪浪环境科技股份有限公司 | A kind of incinerator smoke takes the devices and methods therefor of air-flow removing bioxin |
| CN108443889A (en) * | 2018-02-28 | 2018-08-24 | 上海锅炉厂有限公司 | A kind of discarded metal catalyst and organic sludge coprocessing device and method |
| CN108443889B (en) * | 2018-02-28 | 2023-08-08 | 上海锅炉厂有限公司 | Waste metal catalyst and organic sludge co-treatment device and method |
| CN108826319A (en) * | 2018-08-16 | 2018-11-16 | 东华工程科技股份有限公司 | Dangerous waste incinerator with dry colling slagging mechanism |
| CN108826319B (en) * | 2018-08-16 | 2023-10-31 | 东华工程科技股份有限公司 | Dangerous waste incinerator with dry cooling slag discharging mechanism |
| CN114135875A (en) * | 2021-11-29 | 2022-03-04 | 广州雅居乐固体废物处理有限公司 | Incineration pretreatment process for high-fluorine solid waste |
| CN115028329A (en) * | 2022-07-11 | 2022-09-09 | 沈阳理工大学 | Comprehensive utilization method and system for thermal catalytic decomposition, separation and drying of sludge flue gas |
| CN115028329B (en) * | 2022-07-11 | 2023-08-11 | 沈阳理工大学 | Comprehensive utilization method and system for thermal catalytic decomposition, separation and drying of sludge flue gas |
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