CN211620348U - Biochemical sludge treatment system - Google Patents
Biochemical sludge treatment system Download PDFInfo
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- CN211620348U CN211620348U CN201922275576.XU CN201922275576U CN211620348U CN 211620348 U CN211620348 U CN 211620348U CN 201922275576 U CN201922275576 U CN 201922275576U CN 211620348 U CN211620348 U CN 211620348U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
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Abstract
The utility model discloses a biochemical sludge treatment system, concretely relates to sludge treatment technical field, processing system are including consecutive sludge drying device, pyrolysis device and combustible gas processing system, sludge drying device is connected with sewage treatment system, sludge drying device is including heating screw conveyer and low temperature belt drier, heating screw conveyer carries the mud of slivering through the slivering machine in the low temperature belt drier, low temperature belt drier will do the mud transportation and arrive among the pyrolysis device. Use the utility model discloses a processing system handles mud, becomes the general discarded object from dangerous waste management with biochemical mud and deals with, realizes that the volume of mud handling is minimizing, handles innoxious, utilizes resourceization, operation serialization.
Description
Technical Field
The utility model belongs to the technical field of sludge treatment, concretely relates to biochemical sludge treatment system.
Background
The PTA sludge is biochemical sludge generated by PTA sewage and contains pollutants such as dimethylbenzene, purified terephthalic acid, cobalt, manganese and the like. The PTA sludge yield per year in China is about 25 ten thousand tons. The current environmental protection sector manages and disposes according to hazardous waste. The prior disposal method is externally transported to the outside of the factory for landfill or drying incineration disposal, has higher disposal cost and does not meet the new environmental protection requirement.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a biochemical sludge treatment system can incessantly carry out the processing of volume minimizing, processing innoxious, utilization resourceization, operation serialization to mud, lets the device become petrochemical production technology's component, makes petrochemical enterprise no longer collect on the factory and land the landfill mud outward, no longer takes place the pollution incident that mud caused to save expenses such as collect on the land, transportation, management, reduce the biochemical sludge cost of enterprise processing by multiples.
The utility model provides a following technical scheme:
the utility model provides a biochemical sludge treatment system, is including consecutive sludge drying device, pyrolysis device and combustible gas processing system, the sludge drying device is connected with sewage treatment system, the sludge drying device is including heating screw conveyer and low temperature belt drier, heating screw conveyer carries the mud of slivering through the slivering machine in the low temperature belt drier, low temperature belt drier will dry sludge transport in the pyrolysis device. The sludge is slowly conveyed to the slivering machine by the heating screw conveyor, biochemical sludge is enabled to walk forwards while receiving heat transferred by an external hot air pipeline of the heating screw conveyor, the biochemical sludge is gradually heated, and a small amount of water is separated out; under the continuous driving of the heating screw conveyor, the sludge with reduced moisture reaches the sludge strip forming machine to form strip-shaped sludge. The utility model discloses incessant carry out the volume to mud minimizing, handle innoxious, utilize the resourceization, the processing of operation serialization lets the device become petrochemical production technology's component part, makes the petrochemical industry enterprise no longer collect on land the landfill mud outside the factory, no longer takes place the pollution incident that mud causes to sparingly collect on land, expenses such as transportation, management, reduce the biochemical sludge cost of enterprise's processing by multiples.
Preferably, the pyrolysis device comprises a dry sludge feeder and a gasification furnace, and the low-temperature belt type drying machine transfers dry sludge to the gasification furnace through the dry sludge feeder.
Preferably, the combustible gas processing system includes consecutive hot-blast furnace, gas cleaning system and chimney, the hot-blast furnace with the end of giving vent to anger of gasifier passes through the pipe connection, the hot-blast furnace passes through hot-blast main and does respectively heating screw conveyer, low temperature belt drier with the pyrolysis device heat supply. Organic matter is pyrolyzed into combustible gas, high-temperature air is generated by combustion of a hot blast stove and is circularly used for wet sludge drying and bottom air preheating of a pyrolysis device, so that waste is changed into valuable, and resource utilization is realized.
Preferably, a denitration integrated device and a sensitive catcher are arranged in the flue gas purification system, and the sensitive catcher is used for measuring the components and the production of the flue gas in advance. The tail gas produced in the treatment process is subjected to targeted biochemical treatment by measuring the components and the production of the tail gas in advance through a sensitive catcher, and particularly, the sensitive catcher is arranged at the front end of a flue gas inlet pipeline and is used for measuring the concentration of sulfur components in the gas and determining the amount of ammonia water sprayed by liquid at the rear end of the pipeline. After reaching the standard, the sludge is discharged outside through a chimney with the height of 15 meters, so that the harmless treatment of the sludge is realized, and the technology is a technology which is beneficial to environmental protection, public benefit and environmental compatibility.
Preferably, the sewage treatment system comprises a deodorization condenser and a sewage treatment facility which are connected, the deodorization condenser is connected with the water mist outlet end of the sludge drying device through a pipeline, and the gas outlet end of the deodorization condenser is connected with the combustible gas treatment system.
Preferably, the system further comprises a plurality of monitoring cameras, and the monitoring cameras are used for monitoring the operation condition of the system in real time and transmitting the operation condition to the central control room.
Preferably, all components are arranged in one housing.
A biochemical sludge treatment process specifically comprises the following steps:
s1, adding the sludge with the water content of more than 87% into a receiving hopper of a heating screw conveyor, and preheating the sludge in the conveying process;
s2, processing the preheated sludge into strips through a strip forming machine, and then sending the strips into a low-temperature belt type drier to dry the sludge into granular sludge with the water content of below 20%; sending the condensate water generated by drying into a sewage treatment system in a plant for treatment;
s3, conveying the dried sludge into a gasification furnace through a dry sludge feeder for pyrolysis gasification reaction to produce combustible gas and ash residues;
s4, ash generated by the gasification furnace is consigned to be transported outside for disposal; and the combustible gas is sent into a combustible gas treatment system for treatment.
Preferably, in step S4, the combustible gas enters a hot-blast stove in the combustible gas treatment system for incineration treatment, and the incineration heat is recovered by the hot-blast stove in the form of hot air and then used for preheating the wet sludge and the furnace bottom air of the gasification furnace.
Preferably, the sludge is fully pyrolyzed in an anoxic state, and the pyrolysis temperature of the gasification furnace is 300-750 ℃. Pyrolyzing in an anoxic state to form 4% recyclable ash, and discharging the ash through a conveying device; abundant pyrolysis is a large amount of combustible gases, sends into the hot-blast furnace to combustible gases through pipeline, burns under the ignition of lighter, and the hot-air recovery of burning high temperature carries wet sludge drying and gasifier end wind through the pipeline and preheats to reduce and handle the mud energy consumption. By controlling the pyrolysis temperature of the organic matters, the generation of dioxin in the whole treatment process is effectively controlled.
The utility model has the advantages that:
1. all the parts are arranged in a shell type box body with the floor area of about 60 square meters and are connected with a petrochemical production line to form an organic component of a petrochemical process, so that the sludge is not transported outside, a factory does not need to collect land outside a factory for landfill, and no pollution and environmental protection event occurs, thereby saving the cost of collecting land, transporting, managing and the like and reducing the cost of treating biochemical sludge by enterprises manyfold.
2. The biochemical sludge treatment system can treat biochemical sludge with the water content of 87% by the system, and 4% of recyclable ash residues are left; organic matter is pyrolyzed into combustible gas, high-temperature air is generated by combustion of a hot blast stove and is circularly used for drying wet sludge and preheating bottom air of a gasification furnace, so that waste is changed into valuable, and resource utilization is realized.
3. According to the biochemical sludge treatment system, the generation of dioxin in the whole treatment process is effectively controlled by controlling the pyrolysis temperature of organic matters; the tail gas generated in the treatment is measured in advance through a sensitive catcher, the components and the generation amount of the tail gas are specifically and biochemically treated, and the tail gas is discharged through a chimney with the height of 15 meters after reaching the standard, so that the harmless treatment of the sludge is realized, and the technology is beneficial to environmental protection, public benefit and environmental compatibility.
Drawings
The accompanying drawings are included to provide a further understanding of the invention, and are incorporated in and constitute a part of this specification, illustrate embodiments of the invention, and together with the example serve to explain the invention and not to limit the invention. In the drawings:
FIG. 1 is a schematic diagram of the system of the present invention;
fig. 2 is a schematic diagram of the system of the present invention;
fig. 3 is a heat and material balance diagram of the present invention.
Wherein the figures are labeled: 1. heating the screw conveyor; 2. a slivering machine; 3. a low temperature belt drier; 4. a dry sludge feeder; 5. a gasification furnace; 6. a hot blast stove; 7. a flue gas purification system; 8. a chimney; 9. a hot air circulating fan; 10. a deodorizing condenser.
Detailed Description
Example 1
As shown in fig. 1-2, a biochemical sludge treatment system comprises a sludge drying device, a pyrolysis device and a combustible gas treatment system which are connected in sequence, wherein the sludge drying device is connected with a sewage treatment system and comprises a heating screw conveyor 1 and a low-temperature belt type drying machine 3, and the heating screw conveyor 1 conveys the strip-formed sludge into the low-temperature belt type drying machine 3 through a strip forming machine 2; the pyrolysis device comprises a dry sludge feeder 4 and a gasification furnace 5, and the low-temperature belt type drying machine 3 transfers dry sludge into the gasification furnace 5 through the dry sludge feeder 4. The combustible gas processing system comprises a hot blast stove 6, a flue gas purification system 7 and a chimney 8 which are sequentially connected, the air outlet ends of the hot blast stove 6 and the gasification furnace 5 are connected through a pipeline, and the hot blast stove 6 supplies heat to a heating screw conveyer 1, a low-temperature belt type drier 3 and a pyrolysis device respectively through a hot blast pipeline (if the heat supply is not required, the heat supply in other external modes can be carried out). Organic matter is pyrolyzed into combustible gas (marked as fuel gas in figure 1, which has the same meaning), and high-temperature air is generated by combustion of a hot blast stove 6 and is circularly used for wet sludge drying and bottom air preheating of a pyrolysis device, so that waste is changed into valuable, and resource utilization is realized. The sludge is slowly conveyed to a slivering machine 2 (namely a sludge slivering machine) by a heating screw conveyor 1, biochemical sludge walks forwards while receiving heat transferred by a hot air pipeline outside the heating screw conveyor 1, the biochemical sludge is gradually heated, and a small amount of water is separated out; under the continuous driving of the heating screw conveyor 1, the sludge with reduced moisture reaches the sludge slivering machine 2 to be made into strip-shaped sludge. The utility model discloses incessant carry out the processing of volume minimizing, processing innoxious, operation serialization to mud, let the device become petrochemical production technology's component, make petrochemical industry enterprise no longer collect on the factory and land the landfill mud outward, no longer take place the pollution incident that mud causes to sparingly collect on land, expense such as transportation, management, reduce the biochemical sludge cost of enterprise processing at double.
Specifically, a denitration integrated device and a sensitive catcher are arranged in the flue gas purification system, and the sensitive catcher is used for measuring flue gas components and the output in advance. The tail gas produced in the treatment is measured in advance through a sensitive catcher (a smoke measuring device), the components and the production quantity of the tail gas are specifically treated biochemically, and the tail gas is discharged outwards through a chimney 8 with the height of 15 meters after reaching the standard, so that the harmless treatment of the sludge is realized, and the technology is beneficial to environmental protection and public benefits and environmental affinity.
Specifically, the sewage treatment system comprises a deodorization condenser 10 and a sewage treatment facility which are connected, the deodorization condenser 10 is connected with the water mist outlet end of the low-temperature belt type drier 3 through a pipeline, and the gas outlet end of the deodorization condenser 10 is connected with the combustible gas treatment system. The function of the deodorizing condenser is: the condensable odor can be condensed to form waste water, and the waste water is sent to a sewage treatment facility for treatment; the non-condensable odor is sent into a hot blast stove 6 for high-temperature pyrolysis.
Specifically, the system further comprises a plurality of monitoring cameras, and the monitoring cameras are used for monitoring the operation condition of the system in real time and transmitting the operation condition to the central control room. If the monitoring cameras are arranged at the sludge feeding and discharging port, the observation port of the pyrolysis device (the gasification furnace 5), the slag hole, the key process instrument and the like, the operation condition of the system is monitored in real time and is transmitted to the central control room. A temperature detection thermocouple is arranged in the pyrolysis device, and a temperature signal interlocks and controls a furnace bottom air valve to automatically maintain the gasification state in the furnace; the over-temperature alarm system is arranged, and when abnormal detonation occurs in the device, the air inlet amount is automatically controlled in a linkage manner. An on-line moisture detector is arranged in the sludge drying machine in an automatic control and interlocking device, the moisture content of the sludge is monitored in real time, and a feeding system is controlled in a lock-connected mode, so that the moisture content of discharged sludge is guaranteed to be stably below 20%.
In particular, all components are arranged in one housing. The housing has a floor area of about 60 square meters. A novel pyrolysis (low-temperature drying and pyrolysis gasification) device with compact layout and container type.
Example 2
Taking sludge generated by chemical fiber PTA, wherein the component characteristic of the sludge is 87% of water content, and treating the sludge according to the following process:
a biochemical sludge treatment process specifically comprises the following steps:
s1, adding the sludge with the water content of 87% into a receiving hopper of the heating screw conveyor 1, and preheating the sludge in the conveying process; such that the sludge characteristic is 87% water, about 100 ℃; the sludge is slowly conveyed to the slivering machine 2 by the heating screw conveyor 1, biochemical sludge is enabled to walk forwards and receive heat transferred by a hot air pipeline outside the heating screw conveyor 1 at the same time, so that the biochemical sludge is gradually heated, and a small amount of water is separated out; under the continuous driving of the heating screw conveyor 1, the sludge with reduced moisture reaches the sludge strip forming machine;
s2, processing the preheated sludge into strips through a strip forming machine 2, and then sending the strips into a low-temperature belt type drier 3, specifically strip-shaped sludge falling onto a high-temperature-resistant and corrosion-resistant stainless steel mesh belt of a drying chamber of the low-temperature belt type drier 3, wherein the strip-shaped sludge is in indirect contact with a material through a heat conduction pipe, so that the sludge is uniformly heated under the combined action of a variable-frequency fan and a thermocouple in the low-temperature belt type drier 3, water in the sludge is gradually seeped out in a water mist form at a set temperature, and the water is deodorized and condensed into liquid through a deodorization condenser 10, flows into a sewage collecting pipe, is discharged from a discharge pipe port, and is sent to a sewage treatment plant (sewage treatment facility) for treatment; the sludge with the water content of about 20 percent is conveyed into a pyrolysis device (a gasification furnace 6) through a sealed conveying pipeline without dust leakage; the odor of the sludge is separated out from the sludge and enters a deodorization steam condenser 10 together with water mist under the temperature action of a drying chamber of a low-temperature belt type drier 3, and the uncondensable odor is absorbed by a draught fan and a gas collecting pipeline and is sent into a hot blast stove 6 for combustion, then the sludge enters a flue gas purification system 7 for treatment, and the sludge is discharged through a chimney with the height of 15 meters after reaching the emission standard.
S3, conveying the dried sludge into a gasification furnace 5 through a dry sludge feeder 4 for pyrolysis gasification reaction to produce combustible gas and ash;
s4, ash generated by the gasification furnace 5 is entrusted to be transported outside, and the ash is about 550 ℃; and the combustible gas is sent into a combustible gas treatment system for treatment.
Specifically, the sludge is fully pyrolyzed in an anoxic state, and the pyrolysis temperature of the gasification furnace 5 is 300-750 ℃. Pyrolyzing in an anoxic state to form 4% recyclable ash, and discharging the ash through a conveying device; abundant pyrolysis is a large amount of combustible gases, sends into hot-blast furnace 6 to the combustible gas through pipeline, burns under the ignition of lighter, and the hot-air recovery of burning high temperature carries wet sludge drying and 5 end wind preheats of gasifier through the pipeline to reduce and handle the mud energy consumption. By controlling the pyrolysis temperature of the organic matters, the generation of dioxin in the whole treatment process is effectively controlled.
Materials and heat in the sludge treatment process are shown in figure 3, the hourly conveying amount of the sludge on the heating screw conveyor 1 is 625kg/h, the water content is 87 percent, and the temperature is 20 ℃; the conveying capacity per hour in a slivering machine is 625kg/h, the water content is 87 percent, and the temperature is about 100 ℃; the hourly conveying capacity of the low-temperature belt type drying machine is 523kg/h, and the temperature is 40 ℃. The dried sludge is transported in a pipeline with the hourly conveying capacity of 102kg/h and the water content of 20 percent and the temperature of 40 ℃ and then enters a dry sludge feeder 4, the hourly conveying capacity of the dry sludge feeder 4 is 102kg/h and the water content of 20 percent and the temperature of 40 ℃ and then is sent into a gasification furnace 5. The delivery quantity of hot air provided by the hot blast stove 6 is 129kg/h, the temperature is 250 ℃, the delivery quantity of combustible gas generated by the gasification furnace 5 and sent to the hot blast stove 6 is 199kg/h, 450 ℃, and the output quantity of generated ash is 32kg/h and 550 ℃.
Calculating the energy saving rate of the preheated sludge:
sludge drying heat requirement = (40 ℃ saturated steam enthalpy-20 ℃ hot water enthalpy) × 0.87
=（2568.7kj/kg-83.9kj/kg）×0.87=2162kj/kg
The sludge needs heat quantity when being preheated to 100 ℃ (= (the enthalpy value of saturated hot water at 100 ℃ -20 ℃) multiplied by 0.87
=（419.1kj/kg-83.9kj/kg） × 0.87=292kj/kg
The drying energy saving rate is 1- (2162kj/kg-292kj/kg)/2162kj/kg =14%
Sludge reduction rate = (625 kg/h-32 kg/h)/625 kg/h =95%
The utility model has the advantages that:
1. and (3) large decrement: the secondary drying and gasification secondary decrement process is adopted to realize the decrement of wet sludge by more than 95 percent;
2. the energy consumption is low: the wet sludge is preheated by the heat of the dry sludge gasified combustible gas, so that the sludge drying energy consumption is reduced by about 15 percent
3. No pollution: waste gas and dust are not generated in the process of sludge drying; organic matters are converted into combustible gas, and no odor exists; pollutants such as heavy metals and the like are solidified in the ash without diffusion;
4. the structure is simple: the three-machine two-furnace has simple structure, short manufacturing period and low operation and maintenance cost;
5. the occupied area is small: the whole process occupies about 60m of land2The arrangement is compact;
6. manufacturing according to the requirements: the integrated equipment can be customized according to conditions such as sludge yield, site conditions, sludge components and the like.
The above description is only the specific implementation manner of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art can substitute or change the technical solution of the present invention and the design of the present invention within the technical scope of the present invention.
Claims (7)
1. The utility model provides a biochemical sludge treatment system, its characterized in that, is including consecutive sludge drying device, pyrolysis device and combustible gas processing system, the sludge drying device is connected with sewage treatment system, the sludge drying device is including heating screw conveyer and low temperature belt drier, heating screw conveyer carries the mud of slivering through the slivering machine in the low temperature belt drier, low temperature belt drier will do sludge transport to in the pyrolysis device.
2. The biochemical sludge treatment system according to claim 1, wherein the pyrolysis device comprises a dry sludge feeder and a gasifier, and the low-temperature belt drier transfers dry sludge into the gasifier through the dry sludge feeder.
3. The biochemical sludge treatment system according to claim 2, wherein the combustible gas treatment system comprises a hot blast stove, a flue gas purification system and a chimney which are connected in sequence, the air outlet ends of the hot blast stove and the gasification furnace are connected through a pipeline, and the hot blast stove supplies heat to the heating screw conveyer, the low-temperature belt type drying machine and the pyrolysis device through hot blast pipelines respectively.
4. The biochemical sludge treatment system according to claim 3, wherein a denitration integrated device and a sensitive catcher are arranged in the flue gas purification system, and the sensitive catcher is used for measuring the components and the production amount of the flue gas in advance.
5. The biochemical sludge treatment system according to claim 1, wherein the sewage treatment system comprises a deodorization condenser and a sewage treatment facility which are connected, the deodorization condenser is connected with the water mist outlet end of the sludge drying device through a pipeline, and the gas outlet end of the deodorization condenser is connected with the combustible gas treatment system.
6. The biochemical sludge treatment system according to claim 1, further comprising a plurality of monitoring cameras for monitoring the operation condition of the system in real time and transmitting to the central control room.
7. The biochemical sludge treatment system according to any one of claims 1 to 6, wherein all the components are provided in one housing.
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| CN201922275576.XU CN211620348U (en) | 2019-12-18 | 2019-12-18 | Biochemical sludge treatment system |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113045176A (en) * | 2021-04-06 | 2021-06-29 | 河南城建学院 | Energy-saving sludge drying device for recovering waste heat |
| CN113072283A (en) * | 2019-12-18 | 2021-07-06 | 张连发 | Biochemical sludge treatment system and treatment process thereof |
| DE202022104468U1 (en) | 2022-08-05 | 2022-08-19 | Manjeet Singh Barwa | A novel IoT-based sustainable system for treating medical waste |
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2019
- 2019-12-18 CN CN201922275576.XU patent/CN211620348U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113072283A (en) * | 2019-12-18 | 2021-07-06 | 张连发 | Biochemical sludge treatment system and treatment process thereof |
| CN113045176A (en) * | 2021-04-06 | 2021-06-29 | 河南城建学院 | Energy-saving sludge drying device for recovering waste heat |
| CN113045176B (en) * | 2021-04-06 | 2022-06-21 | 河南城建学院 | Energy-saving sludge drying device for recovering waste heat |
| DE202022104468U1 (en) | 2022-08-05 | 2022-08-19 | Manjeet Singh Barwa | A novel IoT-based sustainable system for treating medical waste |
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