CN208604069U - A kind of useless organic matter comprehensive utilization processing system - Google Patents
A kind of useless organic matter comprehensive utilization processing system Download PDFInfo
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- CN208604069U CN208604069U CN201821125031.XU CN201821125031U CN208604069U CN 208604069 U CN208604069 U CN 208604069U CN 201821125031 U CN201821125031 U CN 201821125031U CN 208604069 U CN208604069 U CN 208604069U
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Abstract
The utility model relates to a kind of useless organic matters to comprehensively utilize processing system, belong to resource reclaim processing technology field, it provides a kind of easy to operate, it can be effectively by biochemical sludge, the industry waste organic matter such as spent organic solvent is converted into synthesis gas and low-pressure steam, it is useless organic matter comprehensive utilization processing system without secondary pollution, it is specific to use first by useless solid organic matter, waste liquid state organic matter, additive and breeze carry out mixed grinding according to a certain percentage, form coal-water-oil slurry, then coal-water-oil slurry is entered gasification furnace progress high-temperature gasification with oxygen mix to react, the synthesis gas that reaction generates obtains pure synthesis gas after gas washing purifies, the Heisui River that gas washing generates forms fine slag filter cake through flash distillation filtering, whole process is without secondary pollution, effectively Industry Waste organic matter can be handled, and synthesis gas (the H generated2And CO) and low-pressure steam, it can be used as industrial chemicals, guarantee that resource makes full use of.
Description
Technical field
The utility model relates to a kind of useless organic matters to comprehensively utilize processing system, belong to resource reclaim processing technology field.
Background technique
Useless organic matter is divided into give up organic matter and liquid of solid-state and gives up organic matter, wherein solid-state is given up organic matter such as greasy filth dross, life
Change sludge, liquid give up organic matter such as smart (steaming) evaporate residue, waste mineral oil, waste emulsified mixture, weigh alcohol, light alcohol burning is now external
A kind of processing disposal options approved, but have as the raising of environment protectment protection and burning are also easy to produce dioxin-like chemical etc.
Malicious pernicious gas, also by the query of people；The exhaust gas volumn that solid waste burning technique generates simultaneously is big, it is more to endanger ingredient,
It purifies that required equipment investment and operating cost are larger to it, becomes the development bottleneck of engineering application.And the recycling skill that gasifies
It is not only H by useless organic matter transformation that art, which is a kind of,2, industrial raw material or the energy such as CO and low-pressure steam.Gasify recycling
Technology is while useless organic matter is disposed in processing, and by its resource utilization, this is not only without the poisonous and hazardous substance of dioxin
It generates, realizes energy saving environment, while achieving the purpose that waste resource recovery utilizes.
Utility model content
To solve technical problem of the existing technology, the utility model provide it is a kind of easy to operate, can effectively by
The industry waste organic matter such as biochemical sludge, spent organic solvent is converted into unstripped gas (H2And CO) and low-pressure steam, it is without secondary pollution
Useless organic matter comprehensively utilizes processing system.
To achieve the above object, technical solution used by the utility model is a kind of useless organic matter comprehensive utilization processing system
System, including material grinder and gasification furnace, the material grinder are used for breeze, useless solid organic matter, waste liquid state organic matter and additive
It is ground, the discharge end of the material grinder is connected with material grinder blow tank, and the material grinder blow tank passes through grinding machine blow tank
Pump is connected with slurry vessel, and the slurry vessel is pumped by high-pressure slurry to be connected with the process burner of gasification furnace, the gasification furnace
Process burner be also connected with air hose, the crude synthesis gas that the gasification furnace generates enters aeration tower by Venturi scrubber,
The thick slag that the gasification furnace generates is entered by lock hopper removes slag bath, and the hot water inlet of the aeration tower is connected with hot-water tower, described
High pressure grey water pump is connected between hot-water tower and aeration tower, the bottom of the aeration tower is connected with hp flash drum, the high pressure
The top gas outlet of flash tank is connected with hot-water tower, and the bottom of the hp flash drum is connected with vacuum flasher, described true
In the bottom outlet tube insertion subsider of empty flash tank, the top gas outlet of the vacuum flasher is connected with vacuum flashing condensation
Device, the gas outlet of vacuum flashing condenser are connected with vacuum flashing pump, the bottom outlet tube insertion of the vacuum flashing condenser
In ash water tank, the top duct of the ash water tank and subsider is connected, and the ash water tank is by low pressure grey water pump and rinses sink
It is connected, the bottom for rinsing sink is connect with lock hopper, and the bottom of the subsider passes through filter feed pump and vacuum belt
Formula filter is connected, and the filtrate generated except slag bath is pumped into vacuum flasher by slag pool pump.
Preferably, the outlet tube of the vacuum flasher also passes through flocculant pipeline and is connected with flocculant slot, the flocculation
It is provided with flocculant pump on agent pipeline, is also connected with dispersing agent adding tube between the ash water tank and low pressure grey water pump, described point
Powder adding tube is connected with dispersing agent slot, and dispersing agent pump is provided in the dispersing agent adding tube.
It preferably, further include hopper for storing breeze and feed Weighing feeder, the bottom of the hopper and feed
Weighing feeder is connected, and the feed Weighing feeder is connected with material grinder.
Preferably, the gasification furnace uses water-cooling structure, and the outside of the gasification furnace is provided with water-cooling wall drum and boiler
Water-circulating pump.
Compared with prior art, the utility model has following technical effect that the utility model is easy to operate, operating cost
It is low, mixed grinding is proportionally carried out using by useless solid organic matter, waste liquid state organic matter, additive and breeze, forms ternary
Then coal-water-oil slurry is entered gasification furnace progress high-temperature gasification with oxygen mix and reacted, reacts the synthesis gas of generation through washing by slurry
Pure synthesis gas is obtained after gas purification, the Heisui River that gas washing generates forms fine slag filter cake through flash distillation filtering, and whole process is without secondary
Pollution, can effectively be handled Industry Waste organic matter, and the unstripped gas and low-pressure steam generated, can be used as chemical industry original
Material, guarantees that resource makes full use of.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Specific embodiment
In order to which technical problem to be solved in the utility model, technical solution and beneficial effect is more clearly understood, with
Lower combination accompanying drawings and embodiments, the present invention will be further described in detail.It should be appreciated that specific reality described herein
It applies example to be only used to explain the utility model, is not used to limit the utility model.
As shown in Figure 1, a kind of useless organic matter comprehensively utilizes processing system, including be also used to store breeze hopper 1 and to
Expect Weighing feeder 2, material grinder 3 and gasification furnace 7, the bottom of hopper 1 is connected with feed Weighing feeder 2, and feed weighing is given
Material machine 2 is connected with material grinder 3, and material grinder 3 is used to carry out breeze, useless solid organic matter, waste liquid state organic matter and additive
Grinding, the discharge end of material grinder 3 are connected with material grinder blow tank 4, and material grinder blow tank 4 passes through grinding machine blow tank pump 15 and slurry
Slot 5 is connected, and slurry vessel 5 is connected by high-pressure slurry pump 6 with the process burner of gasification furnace 7, and the process burner of gasification furnace 7 is also
It is connected with air hose 9, the crude synthesis gas that gasification furnace 7 generates enters aeration tower 12 by Venturi scrubber 11, and gasification furnace 7 generates
Melt cinder entered by lock hopper 16 and remove slag bath 17, the hot water inlet of aeration tower 12 is connected with hot-water tower 14, hot-water tower 14 and gas washing
High pressure grey water pump 13 is connected between tower 12, the bottom of aeration tower 12 is connected with hp flash drum 24, the top of hp flash drum 24
Portion gas outlet is connected with hot-water tower 14, and the bottom of hp flash drum 24 is connected with vacuum flasher 27, vacuum flasher 27
Bottom outlet tube is inserted into subsider 29, and the top gas outlet of vacuum flasher 27 is connected with vacuum flashing condenser 26, vacuum
The gas outlet of flash condenser 26 is connected with vacuum flashing pump 25, and the bottom outlet tube of vacuum flashing condenser 26 is inserted into ash water tank
In 28, ash water tank 28 is connect with the top duct of subsider 29, and ash water tank 28 passes through low pressure grey water pump 22 and flushing 19 phase of sink
Connection, the bottom for rinsing sink 19 are connect with lock hopper 16, and the bottom of subsider 29 passes through filter feed pump 30 and vacuum belt
Filter 31 is connected, except the filtrate that slag bath 17 generates is pumped into vacuum flasher 27 by slag pool pump 18.
Wherein, the outlet tube of vacuum flasher 27 also passes through flocculant pipeline and is connected with flocculant slot 33, flocculant pipeline
On be provided with flocculant pump 32, be also connected with dispersing agent adding tube between ash water tank 28 and low pressure grey water pump 22, dispersing agent addition
Pipe is connected with dispersing agent slot 20, and dispersing agent pump 21 is provided in dispersing agent adding tube.
When the utility model is specifically used, it is broadly divided into the preparation of ternary waste slurry, gasification furnace gasification, synthesis material air purge
It washs, the several processes of black water flash and fine slag processing.
The preparation of ternary waste slurry: the give up useless organic matter of organic matter, liquid, additive and breeze of solid-state is proportionally added to
In material grinder, material grinder grinds breeze, useless solid, liquid organic matter and additive etc., and slurry storage is formed after the completion of grinding
In slurry vessel.
Gasification furnace gasification: the slurry and oxygen prepared is mixed in proportion, is entered by the process burner of gasification furnace
High-temperature gasification reaction is carried out in gasification furnace.Under the high temperature and high pressure environment of gasification furnace combustion chamber, oxygen and breeze, gasification lime-ash,
Violent reaction occurs for spent organic solvent, solid organic matter, which is one and extremely complex has coupled a series of objects
The process of reason and chemical change, including dehydration point and fugitive constituent → burning → gasification several stages, each stage hand over and infiltrate row.Together
When gasification furnace use water wall structure, the outside of gasification furnace 7 is provided with water-cooling wall drum 10 and boiler water circulating pump 8, makes to gasify
The outside wall temperature of furnace pressure resistance steel shell is maintained at 150 DEG C or so.
Synthesis material gas washing: gas washing is entered by Venturi scrubber from the crude synthesis gas come out from gasification furnace shock chamber
Tower, Venturi scrubber can remove part ash, the impurity such as fine slag in the unstripped gas generated after degassifying.Into the synthesis of aeration tower
Gas initially enters the fine slag that part is washed off in the water of gas washing tower bottom, is then substantially free of the synthesis gas of solid particle along aeration tower
It flows up, the condensate liquid adverse current outside battery limit (BL) being added with the circulation buck and tower top entered in the middle part of tower directly connects
Touching, washs remaining solid particle, leaves dustiness < 1mg/Nm3 in the synthesis gas of aeration tower.It is equipped at the top of aeration tower
Spiral board demister, synthesis gas remove the water mist wherein carried secretly when leaving aeration tower, and clean synthesis gas passes through after going out aeration tower
It crosses control valve and sends out battery limit (BL).On-line gas analysis instrument is installed in the outlet of aeration tower, to CH4、CO、H2And CO2It is examined
It surveys.
Black water flash: enter hp flash drum from the Heisui River that gas washing tower bottom comes.In hp flash drum, a part of water
Become steam through vacuum flashing, high pressure flash steam sends to hot-water tower, recycles heat.The water being discharged from high pressure flash pot bottom contains
There is more solid particle, this part Heisui River is sent to vacuum flasher by Liquid level, and the Heisui River from slag bath is also sent to very
Empty flash tank.By the flash distillation in vacuum flasher, the gas dissolved in Heisui River is released.The sudden strain of a muscle come out from vacuum flasher
Steam initially enters vacuum flashing condenser and is condensed and separated, and the lower liquid of vacuum flashing condenser is inserted directly into ash water tank.
The vacuum degree of vacuum flasher is realized by vacuum pump.Vacuum pump is direct after being drawn out the gas that vacuum flashing condenser comes out
Atmosphere is arranged, liquid removes ash water tank.Vacuum flasher does not control liquid level, and vacuum flasher lower liquid pipe line is inserted directly into sedimentation groove center
Bucket, using the liquid level of subsider as fluid-tight, to guarantee its vacuum degree.The Heisui River of vacuum flasher discharge enters subsider, leads to
It crosses addition flocculant and carries out sedimentation separation, the filter residue after separation forms fine slag filter cake by vacuum band-type filter machine.Subsider point
Clarified solution from generation enters ash water tank, is then sent by pumping to flushing sink, provides flushing to rinse blowdown line and lock hopper
Buck, while dispersing agent is added in pipeline, pipeline and equipment scaling can be effectively prevent.
Fine slag processing: this system gasification recycling unit generate fine slag send outside to be used as brickmaking industry part raw material or
It is used as other utilizations.
The utility model can be used in biochemical sludge, spent organic solvent and waste containing organic solvent, waste mineral oil and contain mine
Object oil waste, oil/water, hydrocarbon/aqueous mixtures or emulsion, essence (steaming) evaporate residue, organic resin class waste, organic cyaniding waste,
The harmless treatment of the industrial wastes such as waste containing phenol, ether-containing waste, other wastes.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Made any modifications, equivalent replacements, and improvements etc., should all wrap in the utility model model within the spirit and principle of utility model
In enclosing.
Claims (4)
1. a kind of useless organic matter comprehensively utilizes processing system, it is characterised in that: including material grinder and gasification furnace, the material grinder is used
It is ground in breeze, useless solid organic matter, waste liquid state organic matter and additive, the discharge end of the material grinder is connected with mill
Material machine blow tank, the material grinder blow tank is pumped by grinding machine blow tank to be connected with slurry vessel, and the slurry vessel passes through high pressure
Shurry pump is connected with the process burner of gasification furnace, and the process burner of the gasification furnace is also connected with air hose, the gasification furnace
The crude synthesis gas of generation enters aeration tower by Venturi scrubber, and the melt cinder that the gasification furnace generates enters slagging-off by lock hopper
Pond, the hot water inlet of the aeration tower are connected with hot-water tower, and high pressure grey water pump, institute are connected between the hot-water tower and aeration tower
The bottom for stating aeration tower is connected with hp flash drum, and the top gas outlet of the hp flash drum is connected with hot-water tower, described
The bottom of hp flash drum is connected with vacuum flasher, and the bottom outlet tube of the vacuum flasher is inserted into subsider, described
The top gas outlet of vacuum flasher is connected with vacuum flashing condenser, and the gas outlet of vacuum flashing condenser is connected with vacuum sudden strain of a muscle
Pump is steamed, the bottom outlet tube of the vacuum flashing condenser is inserted into ash water tank, the top duct of the ash water tank and subsider
Connection, the ash water tank are connected by low pressure grey water pump with sink is rinsed, and the bottom for rinsing sink is connect with lock hopper, institute
The bottom for stating subsider is connected by filter feed pump with vacuum band-type filter machine, and the filtrate generated except slag bath passes through
Slag pool pump is pumped into vacuum flasher.
2. a kind of useless organic matter according to claim 1 comprehensively utilizes processing system, it is characterised in that: the vacuum flashing
The outlet tube of tank also passes through flocculant pipeline and is connected with flocculant slot, and flocculant pump is provided on the flocculant pipeline, described
Dispersing agent adding tube is also connected between ash water tank and low pressure grey water pump, the dispersing agent adding tube is connected with dispersing agent slot,
Dispersing agent pump is provided in the dispersing agent adding tube.
3. a kind of useless organic matter according to claim 1 comprehensively utilizes processing system, it is characterised in that: further include for storing up
The hopper and feed Weighing feeder of breeze are deposited, the bottom of the hopper is connected with feed Weighing feeder, and the feed claims
Weight batcher is connected with material grinder.
4. a kind of useless organic matter according to claim 1 comprehensively utilizes processing system, it is characterised in that: the gasification furnace is adopted
With water-cooling structure, the outside of the gasification furnace is provided with water-cooling wall drum and boiler water circulating pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821125031.XU CN208604069U (en) | 2018-07-17 | 2018-07-17 | A kind of useless organic matter comprehensive utilization processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821125031.XU CN208604069U (en) | 2018-07-17 | 2018-07-17 | A kind of useless organic matter comprehensive utilization processing system |
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| Publication Number | Publication Date |
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| CN208604069U true CN208604069U (en) | 2019-03-15 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821125031.XU Active CN208604069U (en) | 2018-07-17 | 2018-07-17 | A kind of useless organic matter comprehensive utilization processing system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110283630A (en) * | 2019-07-27 | 2019-09-27 | 河南心连心化学工业集团股份有限公司 | Coal chemical industry solid waste treatment device and treatment method |
| CN111185460A (en) * | 2020-01-06 | 2020-05-22 | 杰瑞邦达环保科技有限公司 | Resource utilization process for organic hazardous waste |
-
2018
- 2018-07-17 CN CN201821125031.XU patent/CN208604069U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110283630A (en) * | 2019-07-27 | 2019-09-27 | 河南心连心化学工业集团股份有限公司 | Coal chemical industry solid waste treatment device and treatment method |
| CN111185460A (en) * | 2020-01-06 | 2020-05-22 | 杰瑞邦达环保科技有限公司 | Resource utilization process for organic hazardous waste |
| CN111185460B (en) * | 2020-01-06 | 2021-09-24 | 杰瑞邦达环保科技有限公司 | Resource utilization process for organic hazardous waste |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Hao Gengjian Inventor after: Zhou Wenjia Inventor after: Zhao Guangwu Inventor before: Hao Gengjian Inventor before: Zhao Guangwu |