CN111995201A - Sludge treatment system - Google Patents
Sludge treatment system Download PDFInfo
- Publication number
- CN111995201A CN111995201A CN201910445347.XA CN201910445347A CN111995201A CN 111995201 A CN111995201 A CN 111995201A CN 201910445347 A CN201910445347 A CN 201910445347A CN 111995201 A CN111995201 A CN 111995201A
- Authority
- CN
- China
- Prior art keywords
- product
- unit
- sludge
- reaction
- decomposition
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/10—Treatment of sludge; Devices therefor by pyrolysis
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention discloses a sludge treatment system. The reaction system comprises a raw material conveying unit, a decomposition cracking reaction unit, a reforming synthesis reaction unit, a cooling unit, a product separation unit and a product tank. The raw material conveying unit is connected with the decomposition cracking reaction unit; the decomposition cracking reaction unit is connected with the reforming synthesis reaction unit; the reforming synthesis reaction unit is connected with the cooling unit, the cooling unit is connected with the product separation unit, and the product separation unit is connected with the product tank. The continuous sludge treatment reaction system provided by the invention can realize continuous harmless treatment of sludge, greatly reduces the volume of sludge, can greatly relieve the current sludge treatment dilemma, and has wide application prospects.
Description
Technical Field
The invention belongs to the field of organic solid waste treatment, and particularly relates to a sludge treatment system.
Background
Sludge is a byproduct produced in the process of treating urban domestic sewage and industrial wastewater. In recent years, the municipal sewage treatment industry has been rapidly developed, and biological treatment techniques are being widely used, resulting in a great increase in sludge production. On the other hand, the sludge has the characteristics of high water content, easy decay and strong odor, and contains substances such as parasitic ova, pathogenic microorganisms, heavy metals and the like. The random discharge of the substances can cause secondary pollution to the environment, and the effective treatment and disposal of the sludge are seriously restricted. At present, the sludge disposal modes comprise sanitary landfill, ocean dumping, incineration and the like, and the sanitary landfill has the advantages of low investment, quick effect, large capacity and the like, and is the sludge disposal mode mainly adopted in China at present. However, the sludge landfill area is large, and the landfill leachate has a large amount of heavy metals and refractory organic matters, so that soil and underground water are easily polluted. Furthermore, the sludge in the landfill site is subjected to anaerobic fermentation to generate a large amount of methane, and if measures are not taken properly, explosion and fire are likely to occur. On this basis, the sanitary landfill treatment of sludge is subject to great use restrictions.
One solution to the above problem is to treat the sludge by thermochemical conversion techniques. After heat treatment, the conversion rate of organic matters in the sludge reaches over 90 percent, and the volume is reduced by over 80 percent. But the relevant studies were all carried out in batch reactors. The intermittent operation has the problems of complex operation caused by repeated disassembly of the device, high energy consumption caused by repeated heating and cooling, limited daily treatment capacity and the like, and greatly limits the further popularization and application of the thermochemical conversion of the sludge. To further generalize the use of sludge thermochemical conversion technology, continuous plants need to be developed. At present, researches on a sludge thermochemical conversion reaction device are few, and no scheme is provided for better realizing the thermochemical conversion of the sludge.
Disclosure of Invention
The invention aims to provide a sludge treatment system, which can continuously treat sludge and realize the harmlessness and reduction of sludge treatment.
The system for treating sludge provided by the invention comprises a raw material conveying unit 1, a decomposition cracking reaction unit 9, a reforming synthesis reaction unit 11, a cooling unit 15, a product separation unit 16 and a product tank 17; wherein the raw material conveying unit 1 is connected with the decomposition cracking reaction unit 9; the decomposition cracking reaction unit 9 is connected with the reforming synthesis reaction unit 11; the reforming synthesis reaction unit 11 is connected to the cooling unit 15; the cooling unit 15 is connected with the product separation unit 16; the product separation unit 16 is connected to the product tank 17.
In the above reaction system, the raw material conveying unit 1 includes a raw material storage tank 1 and a solid semi-solid raw material propeller 3;
the discharge port of the raw material storage tank 1 is connected with the feed port of the solid semi-solid raw material propeller 3, and the discharge port of the solid semi-solid raw material propeller 3 is connected with the feed port of the decomposition cracking reaction device 9;
the decomposition cracking reaction unit comprises a decomposition cracking reaction device 9 and a pump 10; the discharge hole of the decomposition cracking reaction device 9 is connected with the feed inlet of the pump 10; the discharge hole of the pump 10 is connected with the feed hole of the reforming synthesis reaction device 11;
the reforming synthesis reaction unit includes the reforming synthesis reaction device 11; the discharge port of the reforming synthesis reaction device 11 is connected with the feed port of a product pipe 14;
the cooling unit comprises a cooling device 15, a product pipe 14 and a back pressure valve 19; the discharge hole of the product 14 is connected with the feed hole of the back pressure valve 19;
the product separation unit 16 comprises a gas collection tank 18, a waste collection tank 20, a product separation device 16; the feed inlet of the product separation device 16 is connected with the discharge outlet of the backpressure valve 19; the discharge port of the product separation device 16 is connected with the product tank 17;
the product separation device 16 specifically comprises a feeding hole, a discharging hole, a gas emptying valve 22 and a waste discharge valve 21; the gas emptying valve 22 of the product separation device is connected with the feed inlet of the gas collection tank 20, and the waste discharge valve 21 of the product separation device 16 is connected with the feed inlet of the waste collection tank 20.
The sludge is human sludge and/or livestock sludge.
When the sludge is used as a raw material, the water content is 1-99%. Specifically 80 percent;
the reaction temperature of the decomposition cracking reaction device is between 100 ℃ and 250 ℃, specifically 160 ℃ to 180 ℃ or 245 ℃, and the reaction residence time is 1 to 2880 min; specifically 30min-45 min;
the reaction temperature of the reforming synthesis reaction device is between 250 ℃ and 500 ℃; the temperature can be 270-400 ℃ or 380 ℃; the reaction residence time is between 1 and 2880 min. Specifically 15min-45min or 120 min;
the decomposition cracking reaction device also comprises a temperature control system and a pressure gauge so that the biomass can react at a set temperature in the decomposition cracking reaction device;
the reforming synthesis reaction device also comprises a temperature control system and a pressure gauge, so that the decomposition cracking products can be subjected to reforming synthesis reaction at a set temperature in the reforming synthesis reaction device to generate products.
Specifically, the decomposition cracking reaction device is divided into two parts, a valve for materials to pass through is arranged at the joint of the two parts in the reactor, the two parts outside the reactor are connected through a balance pipeline, and the balance pipeline is provided with a balance valve; the top is provided with a gas emptying valve.
The feed inlet and the discharge outlet of the cooling unit are respectively provided with a temperature measuring device so as to monitor the temperature of the feed inlet and the discharge outlet of the cooling unit in real time and ensure that the temperature of the discharge outlet is lower than 100 ℃ by adjusting the flow of the coolant.
In addition, the application of the reaction system provided by the invention in the continuous sludge treatment also belongs to the protection scope of the invention.
The invention also claims a method for continuous treatment of sludge, comprising:
conveying sludge in a raw material storage tank of the reaction system into the decomposition cracking reaction device through the solid semi-solid material propeller, heating to 100-250 ℃, and staying for 1-2880min to obtain decomposition liquid (namely decomposition cracking reaction liquid);
conveying the decomposition liquid into the reforming synthesis reaction device through the pump, heating to the temperature of 250-500 ℃, and staying for 1-2880min to obtain a product;
and then the product enters the cooling unit, the temperature is reduced to be below 100 ℃ through cooling, the product with the temperature reduced to be below 100 ℃ enters the product separation unit through the back pressure valve, the gas product enters the gas collection tank through separation, the water phase product and the solid residue enter the waste material collection tank through the waste material discharge valve, and the organic product enters the product tank.
Compared with the prior art, the invention has the following beneficial technical effects:
(1) the invention provides an environment-friendly sludge continuous treatment reaction system which comprises a raw material conveying unit, a decomposition and cracking reaction unit, a reforming and synthesis reaction unit, a cooling unit, a product separation unit and a product tank, wherein the raw material conveying unit is connected with the decomposition and cracking reaction unit; the sludge as the raw material enters a decomposition cracking reaction unit through a raw material conveying unit to generate decomposition cracking reaction to generate a decomposition liquid; delivering the decomposition liquid into a reforming synthesis reaction unit through a pump, and carrying out a reforming synthesis reaction to generate a product; the generated product enters a cooling unit, and is cooled to below 100 ℃ after water cooling; the cooled product enters a product separation unit through a backpressure valve, wherein a gas product enters a gas collection tank through a gas emptying valve; the water phase product and the solid residue enter a waste collecting tank through a waste discharge valve; the organic matter enters the product tank through a discharge port of the product separation device. The invention can efficiently realize the continuous thermochemical conversion of the sludge, so that the whole sludge continuous treatment reaction system has stable and reliable operation and high reaction efficiency.
(2) The reaction system can directly and continuously treat the raw materials without pretreatment; wherein the solid and semi-solid material propeller can convey solid, semi-solid and liquid materials; the arrangement of the decomposition cracking reaction device can realize the liquefaction of the sludge in the decomposition cracking reaction device, enhance the fluidity of the sludge and facilitate the transportation; the arrangement of the reforming synthesis reaction device can lead the micromolecule organic matters in the decomposed liquid to be reunited into hydrocarbon organic matters and organic matters containing N/O/S heteroatoms, reduce the BOD and COD of the treated wastewater and reduce the pressure of subsequent wastewater treatment; the solid and semisolid material propeller and the pump are provided with a variable frequency controller; the control of the feeding amount and the material flow in the system is realized through a solid and semisolid material propeller and a pump; the solid and semi-solid material propeller and the pump are used for adjusting the residence time of the materials in the decomposition cracking reaction device and the reforming synthesis reaction device, so that the whole reaction process is continuous, the reaction of each step is fully carried out, the maximum utilization of organic matters in the sludge can be realized, pathogenic microorganisms and other toxic and harmful substances in the sludge can be fully killed, and finally, the harmless and reduction treatment of the sludge is realized. The cooling unit enables the temperature of the product after passing through the cooling unit to reach below 100 ℃, and the stability of the working environment of the back pressure valve and the safety of the subsequent separation process can be improved.
Drawings
FIG. 1 is a schematic view of a reaction system for continuous treatment of sludge according to the present invention.
The following symbols used in the drawings of the specification are explained as follows:
1 is a raw material tank; 2 is a valve; 3 is a solid and semi-solid material propeller; 4 is a main pipeline; 5 is a balance tube; 6 is a feed valve; 7 is a balance valve; 8 is a gas emptying valve; 9 is a decomposition cracking reaction device; 10 is a pump; 11 is a reforming synthesis reaction device; 12 is a temperature control system; 13 is a pressure gauge; 14 is a product pipe; 15 is a cooling water pipeline; 16 is a product separating tank; 17 is a product tank; 18 is a gas collecting tank; 19 is a back pressure valve; 20 is a waste collecting tank; 21 is a waste discharge valve; and 22 is a gas vent valve.
Detailed Description
The present invention will be further illustrated with reference to the following specific examples, but the present invention is not limited to the following examples. The method is a conventional method unless otherwise specified. The starting materials are commercially available from the open literature unless otherwise specified.
Examples 1,
An environment-friendly reaction system for continuously treating sludge, as shown in fig. 1, comprises a raw material conveying unit 1, a decomposition and cracking reaction unit 9, a reforming and synthesis reaction unit 11, a cooling unit 15, a product separation unit 16 and a product tank 17; wherein the raw material conveying unit 1 is connected with the decomposition cracking reaction unit 9; the decomposition cracking reaction unit 9 is connected with the reforming synthesis reaction unit 11; the reforming synthesis reaction unit 11 is connected to the cooling unit 15; the cooling unit 15 is connected with the product separation unit 16; the product separation unit 16 is connected to the product tank 17.
In the above reaction system, the raw material conveying unit 1 includes a raw material storage tank 1 and a solid semi-solid raw material propeller 3;
the discharge port of the raw material storage tank 1 is connected with the feed port of the solid semi-solid raw material propeller 3, and the discharge port of the solid semi-solid raw material propeller 3 is connected with the feed port of the decomposition cracking reaction device 9;
the decomposition cracking reaction unit comprises a decomposition cracking reaction device 9 and a pump 10; the discharge hole of the decomposition cracking reaction device 9 is connected with the feed inlet of the pump 10; the discharge hole of the pump 10 is connected with the feed hole of the reforming synthesis reaction device 11;
the reforming synthesis reaction unit includes the reforming synthesis reaction device 11; the discharge port of the reforming synthesis reaction device 11 is connected with the feed port of a product pipe 14;
the cooling unit comprises a cooling device 15, a product pipe 14 and a back pressure valve 19; the discharge hole of the product 14 is connected with the feed hole of the back pressure valve 19;
the product separation unit 16 comprises a gas collection tank 18, a waste collection tank 20, a product separation device 16; the feed inlet of the product separation device 16 is connected with the discharge outlet of the backpressure valve 19; the discharge port of the product separation device 16 is connected with the product tank 17;
the product separation device 16 specifically comprises a feeding hole, a discharging hole, a gas emptying valve 22 and a waste discharge valve 21; the gas emptying valve 22 of the product separation device is connected with the feed inlet of the gas collection tank 20, and the waste discharge valve 21 of the product separation device 16 is connected with the feed inlet of the waste collection tank 20.
Example 2: continuous treatment of excess sludge using the reaction System described in example 1
1) Conveying residual sludge with water content of 80% stored in a raw material storage tank 1 into a decomposition cracking reaction device 9 through a solid semi-solid material propeller 3, heating the residual sludge through a temperature control device, heating the sludge in the decomposition cracking reaction device 9 to 200 ℃, and staying in the decomposition cracking reaction device 9 for 30 min; the sludge is converted into decomposition liquid through decomposition cracking reaction;
2) delivering the decomposition liquid into a reforming synthesis reaction device 11 through a pump 10, heating to 310 ℃ through a temperature control device, and staying in the reforming synthesis reaction device 11 for 30 min; converting the decomposition liquid into a product through reforming synthesis reaction;
3) the product generated in the reforming synthesis reaction device 11 enters a cooling device 15 through a discharge hole of the reforming synthesis reaction device, and the temperature of the product at a water outlet of the cooling device 15 is 90 ℃ after cooling;
4) the product cooled to 90 ℃ enters the product separation unit 16 through the back pressure valve 19, and the product is divided into four types: gaseous products, aqueous phase products, organic products, solid residues.
5) The gas product enters a gas collection tank 18, and the water phase product and the solid residue enter a waste material collection tank 20; the organic product enters the product tank 17. The organic products are mainly hydrocarbon substances and organic substances containing N/O/S heteroatoms.
After the treatment, pathogenic microorganisms in the sludge are completely killed, the conversion rate of organic matters in the sludge reaches 83%, the volume of solid residues is only 13% of the original volume of the sludge, and the environment cannot be polluted.
Example 3 continuous treatment of riverbed sludge Using the reaction System described in example 1
1) Conveying residual sludge with the water content of 90% stored in the raw material storage tank 1 to a decomposition cracking reaction device 9 through a solid semi-solid material propeller 3, heating the residual sludge through a temperature control device, heating the sludge in the decomposition cracking reaction device 9 to 170 ℃, and staying in the decomposition cracking reaction device 9 for 30 min; converting the river bed bottom mud into decomposition liquid through decomposition cracking reaction;
2) delivering the decomposition liquid into a reforming synthesis reaction device 11 through a pump 10, heating to 370 ℃ through a temperature control device, and staying for 45min in the reforming synthesis reaction device 11; converting the decomposition liquid into a product through reforming synthesis reaction;
3) the product generated in the reforming synthesis reaction device 11 enters a cooling device 15 through a discharge hole of the reforming synthesis reaction device 11, and the temperature of the product at a water outlet of the cooling device 15 is 90 ℃ after cooling;
4) the product cooled to 90 ℃ enters the product separation unit 16 through the back pressure valve 19, and the product is divided into four types: gaseous products, aqueous phase products, organic products, solid residues.
5) The gas product enters a gas collection tank 18, and the water phase product and the solid residue enter a waste material collection tank 20; the organic product enters the product tank 17. The organic products are mainly hydrocarbon substances and organic substances containing N/O/S heteroatoms.
Through the treatment, microorganisms in the riverbed bottom sludge are killed, the conversion rate of organic matters in the riverbed bottom sludge is 93%, the volume of solid residues is 14% of the original volume, and the pollution risk to the environment is avoided.
Example 4 continuous treatment of granular sludge Using the reaction System described in example 1
1) Conveying the granular sludge with the water content of 60% stored in the raw material storage tank 1 into a decomposition cracking reaction device 9 through a solid semi-solid material propeller 3, heating the granular sludge through a temperature control device, heating the cow dung in the decomposition cracking reaction device 9 to 220 ℃, and staying in the decomposition cracking reaction device 9 for 30 min; the cow dung is converted into decomposition liquid through decomposition cracking reaction;
2) delivering the decomposition liquid into a reforming synthesis reaction device 11 through a pump 10, heating to 350 ℃ through a temperature control device, and staying for 60min in the reforming synthesis reaction device 11; converting the decomposition liquid into a product through reforming synthesis reaction;
3) the product generated in the reforming synthesis reaction device 11 enters a cooling device 15 through a discharge hole of the reforming synthesis reaction device 11, and the temperature of the product at the water outlet of the cooling device 15 is 90 ℃ after cooling;
4) the product cooled to 90 ℃ enters the product separation unit 16 through the back pressure valve 19, and the product is divided into four types: gaseous products, aqueous phase products, organic products, solid residues.
5) The gas product enters a gas collection tank 18, and the water phase product and the solid residue enter a waste material collection tank 20; the organic product enters the product tank 17. The organic products are mainly hydrocarbon substances and organic substances containing N/O/S heteroatoms.
After the reaction, pathogenic microorganisms in the granular sludge are killed, the conversion rate of organic matters in the granular sludge is 95%, the volume of solid residues is 8% of the original volume, and the granular sludge does not have the risk of environmental pollution.
Claims (10)
1. A reaction system for sludge treatment comprises a raw material conveying unit, a decomposition cracking reaction unit, a reforming synthesis reaction unit, a cooling unit, a product separation unit and a product tank; wherein the raw material conveying unit is connected with the decomposition cracking reaction unit; the decomposition cracking reaction unit is connected with the reforming synthesis reaction unit; the reforming synthesis reaction unit is connected with the cooling unit; the cooling unit is connected with the product separation unit; the product separation unit is connected with the product tank.
2. The reaction system of claim 1, wherein: the raw material conveying unit comprises a raw material storage tank and a solid semi-solid raw material propeller;
the discharge port of the raw material storage tank is connected with the feed hopper of the solid semisolid raw material propeller, and the discharge port of the solid semisolid raw material propeller is connected with the feed inlet of the decomposition cracking reaction device;
the decomposition cracking reaction unit comprises a decomposition cracking reaction device and a pump; the discharge hole of the decomposition cracking reaction device is connected with the feed inlet of the pump; the discharge hole of the pump is connected with the feed inlet of the reforming synthesis reaction device;
the reforming synthesis reaction unit comprises the reforming synthesis reaction device; the discharge hole of the reforming synthesis reaction device is connected with the feed inlet of the product pipe;
the cooling unit comprises a cooling device, a product pipe and a back pressure valve; the discharge hole of the product pipe is connected with the feed hole of the back pressure valve;
the product separation unit comprises a gas collection tank, a waste material collection tank and a product separation device; a feed port of the product separation device is connected with a discharge port of the back pressure valve; the discharge hole of the product separation device is connected with the product tank;
the product separation device specifically comprises a feeding hole, a discharging hole, a gas emptying valve and a waste discharge valve; the gas emptying valve of the product separation device is connected with the feed inlet of the gas collection tank, and the waste discharge valve of the product separation device is connected with the feed inlet of the waste collection tank.
3. The reaction system according to claim 1 or 2, wherein: the sludge is human sludge and/or livestock sludge.
4. The reaction system according to any one of claims 1 to 3, wherein: when the sludge is used as a raw material, the water content is 1-99%.
5. The reaction system according to any one of claims 1 to 4, wherein: the reaction temperature of the decomposition cracking reaction device is between 100 ℃ and 250 ℃, and the reaction residence time is 1-2880 min;
the reaction temperature of the reforming synthesis reaction device is between 250 ℃ and 500 ℃; the reaction residence time is between 1 and 2880 min.
6. The reaction system according to any one of claims 1 to 5, wherein: the decomposition cracking reaction device also comprises a temperature control system and a pressure gauge;
the reforming synthesis reaction device also comprises a temperature control system and a pressure gauge.
7. The reaction system according to any one of claims 1 to 6, wherein: the decomposition cracking reaction device is divided into two parts, a valve for materials to pass through is arranged at the joint of the two parts in the reactor, the two parts outside the reactor are connected through a balance pipeline, and the balance pipeline is provided with a balance valve; the top is provided with a gas emptying valve.
8. The reaction system according to any one of claims 1 to 7, wherein: the feed inlet and the discharge outlet of the cooling unit are respectively provided with a temperature measuring device, and the temperature of the discharge outlet is lower than 100 ℃ after cooling.
9. Use of the reaction system according to any one of claims 1 to 8 for continuous treatment of sludge.
10. A method for continuous treatment of sludge comprising:
conveying sludge in a raw material storage tank of the reaction system as defined in any one of claims 1 to 8 into the decomposition cracking reaction device through the solid semi-solid material propeller, heating to 100-250 ℃ and staying for 1-2880min to obtain a decomposition liquid;
conveying the decomposition liquid into the reforming synthesis reaction device through the pump, heating to the temperature of 250-500 ℃, and staying for 1-2880min to obtain a product;
and then the product enters the cooling unit, the temperature is reduced to be below 100 ℃ through cooling, the product with the temperature reduced to be below 100 ℃ enters the product separation unit through the back pressure valve, the gas product enters the gas collection tank through separation, the water phase product and the solid residue enter the waste material collection tank through the waste material discharge valve, and the organic product enters the product tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910445347.XA CN111995201B (en) | 2019-05-27 | 2019-05-27 | Sludge treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910445347.XA CN111995201B (en) | 2019-05-27 | 2019-05-27 | Sludge treatment system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN111995201A true CN111995201A (en) | 2020-11-27 |
| CN111995201B CN111995201B (en) | 2022-11-08 |
Family
ID=73461585
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910445347.XA Active CN111995201B (en) | 2019-05-27 | 2019-05-27 | Sludge treatment system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN111995201B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115286195A (en) * | 2022-08-17 | 2022-11-04 | 中国人民大学 | Environment-friendly reaction device for continuously treating excrement |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5736053A (en) * | 1995-07-27 | 1998-04-07 | Taiyo Oil Co., Ltd. | Method of eliminating mercury from liquid hydrocarbons |
| CN203781995U (en) * | 2013-12-03 | 2014-08-20 | 北京神雾环境能源科技集团股份有限公司 | Sludge treatment system |
| CN104341082A (en) * | 2014-09-30 | 2015-02-11 | 北京久顺科技有限公司 | Sludge oxidation treatment process and device |
| CN104355514A (en) * | 2014-11-06 | 2015-02-18 | 北京绿创生态科技有限公司 | Sludge treatment method based on wet oxidation |
| CN204265697U (en) * | 2014-11-06 | 2015-04-15 | 清华大学 | The device of a kind of continous way two sections of catalyse pyrolysis preparing synthetic gas |
| CN105542808A (en) * | 2016-02-22 | 2016-05-04 | 王志成 | All-closed zero-emission household refuse energy regeneration and comprehensive utilization production process |
| CN107760338A (en) * | 2017-10-24 | 2018-03-06 | 江门绿润环保科技有限公司 | A kind of pyrolysis processing technique of organic solid castoff |
| CN108675604A (en) * | 2018-05-24 | 2018-10-19 | 浙江新技源环境工程有限公司 | A kind of microwave drying, pyrolysis, the method for reforming processing sludge |
-
2019
- 2019-05-27 CN CN201910445347.XA patent/CN111995201B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5736053A (en) * | 1995-07-27 | 1998-04-07 | Taiyo Oil Co., Ltd. | Method of eliminating mercury from liquid hydrocarbons |
| CN203781995U (en) * | 2013-12-03 | 2014-08-20 | 北京神雾环境能源科技集团股份有限公司 | Sludge treatment system |
| CN104341082A (en) * | 2014-09-30 | 2015-02-11 | 北京久顺科技有限公司 | Sludge oxidation treatment process and device |
| CN104355514A (en) * | 2014-11-06 | 2015-02-18 | 北京绿创生态科技有限公司 | Sludge treatment method based on wet oxidation |
| CN204265697U (en) * | 2014-11-06 | 2015-04-15 | 清华大学 | The device of a kind of continous way two sections of catalyse pyrolysis preparing synthetic gas |
| CN105542808A (en) * | 2016-02-22 | 2016-05-04 | 王志成 | All-closed zero-emission household refuse energy regeneration and comprehensive utilization production process |
| CN107760338A (en) * | 2017-10-24 | 2018-03-06 | 江门绿润环保科技有限公司 | A kind of pyrolysis processing technique of organic solid castoff |
| CN108675604A (en) * | 2018-05-24 | 2018-10-19 | 浙江新技源环境工程有限公司 | A kind of microwave drying, pyrolysis, the method for reforming processing sludge |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115286195A (en) * | 2022-08-17 | 2022-11-04 | 中国人民大学 | Environment-friendly reaction device for continuously treating excrement |
Also Published As
| Publication number | Publication date |
|---|---|
| CN111995201B (en) | 2022-11-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102992559B (en) | Method for comprehensively utilizing anaerobic digestion and carbonization of municipal sludge | |
| CN102167486B (en) | Urban sludge, excrement and kitchen garbage combined treatment process | |
| CN103722002B (en) | Based on the consumer waste comprehensively processing method of anaerobic digestion and hydrothermal carbonization | |
| CN102234170B (en) | Method and device for rapidly reducing moisture content of sludge | |
| CN203890193U (en) | Pig farm sewage treatment and biogas production system | |
| CN103224315B (en) | Sludge comprehensive treatment and conversion product recycle method | |
| CN104774044A (en) | Organic waste recycling method and sterilization apparatus used in method | |
| CN107460111A (en) | Organic solid castoff processing system and its method of disposal based on subcritical hydrolysis | |
| CN102603117A (en) | Treatment method of secondary wastewater of kitchen waste | |
| Ahmed et al. | Anaerobic degradation of digestate based hydrothermal carbonization products in a continuous hybrid fixed bed anaerobic filter | |
| CN202543012U (en) | Fluid sludge treatment device for generating clean combustible gas | |
| CN207391399U (en) | Organic solid castoff processing system based on subcritical hydrolysis | |
| CN111995201B (en) | Sludge treatment system | |
| CN203112650U (en) | Kitchen waste wastewater treatment system | |
| CN205295098U (en) | Mud resourceful treatment device | |
| CN213559105U (en) | Urban organic waste cooperative recycling treatment system | |
| CN106673403A (en) | Treatment method of oil sludge | |
| CN201737770U (en) | Microbial response system for waste water treatment and clean energy production at the same time | |
| CN103333716A (en) | Method for preparing hydrogen-rich gas with sludge as raw material and product | |
| CN105645694B (en) | A kind of community's debirs treatment in situ system and method | |
| CN103402930B (en) | The integrated approach of bio oil is prepared by the mud from effluent purifying device | |
| CN109336254B (en) | Novel anaerobic reactor for garbage leachate wastewater treatment | |
| CN203212380U (en) | Anaerobic bioreactor for treating organic wastewater with high solid content | |
| CN216073477U (en) | Pig raising manure treatment and recycling comprehensive utilization system | |
| CN212128002U (en) | Novel organic garbage treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |