CN106701208A - Aerospace gasification furnace ash dreg water comprehensive treatment and utilization method - Google Patents
Aerospace gasification furnace ash dreg water comprehensive treatment and utilization method Download PDFInfo
- Publication number
- CN106701208A CN106701208A CN201710179161.5A CN201710179161A CN106701208A CN 106701208 A CN106701208 A CN 106701208A CN 201710179161 A CN201710179161 A CN 201710179161A CN 106701208 A CN106701208 A CN 106701208A
- Authority
- CN
- China
- Prior art keywords
- water
- ash
- clinker water
- clinker
- gasification furnace
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1625—Integration of gasification processes with another plant or parts within the plant with solids treatment
- C10J2300/1628—Ash post-treatment
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/169—Integration of gasification processes with another plant or parts within the plant with water treatments
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/18—Details of the gasification process, e.g. loops, autothermal operation
- C10J2300/1807—Recycle loops, e.g. gas, solids, heating medium, water
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses an aerospace gasification furnace ash dreg water comprehensive treatment and utilization method, which relates to the technical field of chemical engineering coal ash treatment, and mainly comprises the steps of spraying coal ash to form ash dreg water; carrying out multi-stage suction filtration and solidification on the ash dreg water; stirring in a stock bin; conveying to a boiler for combusting; and the like. According to the aerospace gasification furnace ash dreg water comprehensive treatment and utilization method provided by the invention, the ash dreg water produced in an aerospace gasification furnace of a chemical enterprise is solidified so as to be conveyed to the boiler for recycling and combusting, so that the environment pollution is reduced, and the resource and the production cost are reduced; suction filtered ash water is conveyed to a spraying device through a pipeline so as to be reused, so that the water resource is saved, the discharge of the ash water is reduced, and the environment is further protected; the ash dreg water is subjected to multi-stage suction filtration and solidification so as to form a cake shape, and a solidified filter cake has good quality and an excellent combustion performance, and can be recycled by the boiler.
Description
Technical field
The present invention relates to chemical industry treatment technical field, more specifically a kind of space flight slag from gasifying furnace water synthesis
Disposal and Application way.
Background technology
Space flight gasification furnace be mainly characterized by have the thermal efficiency higher（Up to 95%）And efficiency of carbon con version（Up to 99%）.Boat
Its gasification furnace is water wall structure, can bear 1500 DEG C to 1700 DEG C of high temperature, low to coal requirement, is capable of achieving the local of raw material
Change.The adaptability of coal extensively, from poor lignite, ub-bituminous coal, bituminous coal to petroleum coke can as the raw material of gasification, even
Ash content high, moisture content high, the coal of high-sulfur could be used that it is higher that this allows for space flight gasification furnace coal ash carbon content.Existing treatment
Mode is coal ash is formed clinker water by shower water, then discharges or clinker water is supplied to by centrifugal filtration formation filter cake
It is civilian, be discarded or recycled burning, this processing mode has the following disadvantages：1. the direct discharge of clinker water not only causes serious
Environmental pollution, also wastes substantial amounts of resource, is unfavorable for energy-conserving and environment-protective；2. clinker water forms filter cake by centrifugal filtration, is formed
Filter cake each several part humidity it is uneven, easily cause conveying and block, the solidification of this filter cake is of poor quality in addition, and recovery utilization rate is low,
Efficiency of combustion is low when being burnt for Production in Chemical Plant, and discarded stacking easily causes solid waste pollution, waste of resource, there is provided give
Civilian resource cannot be utilized sufficiently, be unfavorable for cost-effective；3. the buck after lime-ash water filtration is directly discharged, and is wasted
Substantial amounts of water resource, also pollutes environment.How a kind of space flight slag from gasifying furnace water joint disposal method with utilize is designed
It is skill to be solved by this invention to solve the problems, such as that existing treatment is difficult, easily cause environmental pollution and the wasting of resources
Art problem.
The content of the invention
The present invention is in view of the shortcomings of the prior art, there is provided a kind of clinker water suction strainer solidification effect is good, filter cake quality is high has
Help economize on resources and reduce the space flight slag from gasifying furnace water joint disposal and Application way of environmental pollution.
The present invention realizes solving above-mentioned technical problem by following technological means：
A kind of space flight slag from gasifying furnace water joint disposal and Application way, comprise the following steps：
（1）The coal ash that space flight gasification furnace is produced sprays to form clinker water by spray equipment, and the clinker water of formation flow to ash water tank,
Then clinker water is pumped to the buck multistage absorbing devices of clinker water by slush pump.
（2）Clinker water is solidified into pie in the buck multistage absorbing devices of clinker water by multistage suction strainer, clinker water
Buck multistage absorbing devices include clinker water conveyer, negative pressure generator, and negative pressure generator is by clinker water conveyer
Bottom produce negative pressure cause that the buck in clinker water is spun off by suction strainer, the clinker water in the presence of clinker water conveyer
Constantly advance, as the advance of clinker water and the effect of negative pressure generator cause that clinker water forms multistage suction during advancing
Filter, clinker water gradually solidify to form pie, and the buck that suction strainer goes out is used by pipeline to space flight gasification furnace coal ash spray equipment
In the coal ash that space flight gasification furnace is produced is sprayed into clinker water, recycling for water resource is formed.
（3）The coal ash for being solidified into pie is delivered to feed bin by belt conveyor, and stirring motor, pie are provided with feed bin
Coal ash stirred in feed bin and form wet coal ash, wet grey pump is then delivered to by malleation batcher, it is defeated finally by wet grey pump
Boiler is delivered to be burnt.
The advantage of the invention is that：1. space flight slag from gasifying furnace water joint disposal of the invention devises one with Application way
Cover the complete space flight gasification furnace Treatment of Coal Ash that the wet coal ash stirred from coal ash spray humidifying to final curing enters boiler combustion
With utilize flow, the filter cake humidity that clinker water is formed after multistage suction strainer solidifies is uniform, and it is high to reclaim combustion utilization efficiency, solves
Lime-ash water cure is of poor quality, and the low problem of combustion utilization efficiency, space flight slag from gasifying furnace water has obtained effective recycling, saves
Resource and production cost, reduce environmental pollution；2. it is completely embedded between each processing step, can effectively ensures system stream
The stable operation of journey, contributes to the continuous prodution of chemical enterprise, simplifies operation.3. the buck that suction strainer goes out passes through pipeline
Humidifying is carried out to space flight gasification furnace coal ash to spray equipment, the recycling of water resource has been reached, water resource has been saved, reduced
The environmental pollution that buck discharge is caused, is conducive to environmental protection.
Brief description of the drawings
Fig. 1 is the flow chart of space flight slag from gasifying furnace water joint disposal of the invention and Application way.
Specific embodiment
To make the purpose, technical scheme and advantage of the embodiment of the present invention clearer, below in conjunction with the embodiment of the present invention
In accompanying drawing, the technical scheme in the embodiment of the present invention is clearly and completely described, it is clear that described embodiment is
A part of embodiment of the present invention, rather than whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art
The every other embodiment obtained under the premise of creative work is not made, belongs to the scope of protection of the invention.
A kind of space flight slag from gasifying furnace water joint disposal and Application way, comprise the following steps：
（1）The coal ash that space flight gasification furnace is produced sprays to form clinker water by spray equipment, and the clinker water of formation flow to ash water tank,
Then clinker water is pumped to the buck multistage absorbing devices of clinker water by slush pump.
（2）Clinker water is solidified into pie in the buck multistage absorbing devices of clinker water by multistage suction strainer, clinker water
Buck multistage absorbing devices include clinker water conveyer, negative pressure generator, and negative pressure generator is by clinker water conveyer
Bottom produce negative pressure cause that the buck in clinker water is spun off by suction strainer, the clinker water in the presence of clinker water conveyer
Constantly advance, as the advance of clinker water and the effect of negative pressure generator cause that clinker water forms multistage suction during advancing
Filter, clinker water gradually solidify to form pie, and the buck that suction strainer goes out is used by pipeline to space flight gasification furnace coal ash spray equipment
In the coal ash that space flight gasification furnace is produced is sprayed into clinker water, recycling for water resource is formed.
（3）The coal ash for being solidified into pie is delivered to feed bin by belt conveyor, and stirring motor, pie are provided with feed bin
Coal ash stirred in feed bin and form wet coal ash, wet grey pump is then delivered to by malleation batcher, it is defeated finally by wet grey pump
Boiler is delivered to be burnt.
Space flight slag from gasifying furnace water joint disposal of the invention and Application way devise it is a set of from coal ash spray humidifying to
The wet coal ash of final curing stirring enters the complete space flight gasification furnace Treatment of Coal Ash of boiler combustion and utilizes flow, and clinker water leads to
Cross the filter cake humidity formed after multistage suction strainer solidification uniform, it is high to reclaim combustion utilization efficiency, it is of poor quality to solve lime-ash water cure, combustion
The low problem of utilization rate is burnt, space flight slag from gasifying furnace water has obtained effective recycling, saved resource and production cost, drops
Low environmental pollution；It is completely embedded between each processing step, can effectively ensures the stable operation of system flow, contributing to
The continuous prodution of work enterprise, simplifies operation；The buck that suction strainer goes out is by pipeline to spray equipment to space flight gasification furnace
Coal ash carries out humidifying, has reached the recycling of water resource, has saved water resource, reduces the environment dirt that buck discharge is caused
Dye, is conducive to environmental protection.
It should be noted that herein, if being used merely to one in the presence of first and second or the like relational terms
Individual entity or operation make a distinction with another entity or operation, and not necessarily require or imply these entities or operate it
Between there is any this actual relation or order.And, term " including ", "comprising" or its any other variant be intended to
Cover including for nonexcludability, so that process, method, article or equipment including a series of key elements not only include those
Key element, but also other key elements including being not expressly set out, or also include for this process, method, article or set
Standby intrinsic key element.In the absence of more restrictions, the key element limited by sentence "including a ...", it is not excluded that
Also there is other identical element in the process including the key element, method, article or equipment.
The above embodiments are merely illustrative of the technical solutions of the present invention, rather than its limitations；Although with reference to the foregoing embodiments
The present invention has been described in detail, it will be understood by those within the art that：It still can be to foregoing each implementation
Technical scheme described in example is modified, or carries out equivalent to which part technical characteristic；And these modification or
Replace, do not make the spirit and scope of the essence disengaging various embodiments of the present invention technical scheme of appropriate technical solution.
Claims (1)
1. a kind of space flight slag from gasifying furnace water joint disposal and Application way, it is characterised in that comprise the following steps：
（1）The coal ash that space flight gasification furnace is produced sprays to form clinker water by spray equipment, and the clinker water of formation flow to ash water tank,
Then clinker water is pumped to the buck multistage absorbing devices of clinker water by slush pump;
（2）Clinker water is solidified into pie, buck multistage suction strainer in the buck multistage absorbing devices of clinker water by multistage suction strainer
Device includes clinker water conveyer, negative pressure generator, and negative pressure generator is born by being produced in the bottom of clinker water conveyer
Pressure causes that the buck in clinker water is spun off by suction strainer, and clinker water constantly advances in the presence of clinker water conveyer, with
The effect of the advance and negative pressure generator of clinker water causes that clinker water forms multistage suction strainer during advancing, and clinker water is gradually
Pie is solidify to form, the buck that suction strainer goes out passes through pipeline to space flight gasification furnace coal ash spray equipment, for space flight to be gasified
The coal ash that stove is produced sprays into clinker water, forms recycling for water resource;
（3）The coal ash for being solidified into pie is delivered to feed bin by belt conveyor, and stirring motor, the coal of pie are provided with feed bin
Ash stirring in feed bin forms wet coal ash, is then delivered to wet grey pump by malleation batcher, is delivered to finally by wet grey pump
Boiler is burnt.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710179161.5A CN106701208A (en) | 2017-03-23 | 2017-03-23 | Aerospace gasification furnace ash dreg water comprehensive treatment and utilization method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710179161.5A CN106701208A (en) | 2017-03-23 | 2017-03-23 | Aerospace gasification furnace ash dreg water comprehensive treatment and utilization method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106701208A true CN106701208A (en) | 2017-05-24 |
Family
ID=58887134
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710179161.5A Pending CN106701208A (en) | 2017-03-23 | 2017-03-23 | Aerospace gasification furnace ash dreg water comprehensive treatment and utilization method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106701208A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2181983Y (en) * | 1994-03-28 | 1994-11-09 | 武汉市环境保护技术开发中心 | Dust water separating device |
| CN101298569A (en) * | 2008-06-26 | 2008-11-05 | 华东理工大学 | Gasification method of shock chilling type pulp or powder carbonaceous material |
| CN104492587A (en) * | 2014-11-20 | 2015-04-08 | 阜阳市恒宇滤材有限公司 | Comprehensive recycling method for coal slime of space furnace |
-
2017
- 2017-03-23 CN CN201710179161.5A patent/CN106701208A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2181983Y (en) * | 1994-03-28 | 1994-11-09 | 武汉市环境保护技术开发中心 | Dust water separating device |
| CN101298569A (en) * | 2008-06-26 | 2008-11-05 | 华东理工大学 | Gasification method of shock chilling type pulp or powder carbonaceous material |
| CN104492587A (en) * | 2014-11-20 | 2015-04-08 | 阜阳市恒宇滤材有限公司 | Comprehensive recycling method for coal slime of space furnace |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN111068901A (en) | Desilting preposition water-saving energy-saving sand stone aggregate washing system | |
| CN103924624A (en) | Automatic dehydrating dredge boat for riverway sludge and application method of dredge boat | |
| CN110922015A (en) | Harmless treatment method and system for fluid oily sludge | |
| CN105238451A (en) | Efficient combined-type cooling and purifying system for biomass gasification gas | |
| CN102580389B (en) | Method for processing paint slag muck by separating slag muck from water | |
| CN104291548A (en) | Treating method for biochemical sludge and treating device for biochemical sludge | |
| CN104624608A (en) | Recycling and using method of oil-based solid wastes generated by shale gas drilling | |
| CN207471540U (en) | Kitchen castoff and consumer waste incineration coprocessing system | |
| CN106701208A (en) | Aerospace gasification furnace ash dreg water comprehensive treatment and utilization method | |
| CN203048703U (en) | Purification and heat energy recovery system for wastewater of mine sump and coal washing | |
| CN108569834A (en) | A kind of integrated conduct method of domestic sludge | |
| CN204490696U (en) | Oil field slurry containing oil treating device | |
| CN205152031U (en) | Stone material processing sewage slurry treatment device | |
| CN212327767U (en) | Sludge drying machine export tail gas processing system | |
| CN214030655U (en) | Circulating flushing device of belt conveyor | |
| CN210764960U (en) | Combined oil sludge treatment device | |
| KR101533924B1 (en) | Method for Menufacturing Wood-Pellet through Recycling of Wastewood | |
| CN209039312U (en) | The system and device of coal gasification filter cake depth dehydration | |
| CN110848711A (en) | Industrial salt slag pretreatment system | |
| CN219708239U (en) | Adhesive tape cleaning and sewage recycling system | |
| CN205676392U (en) | A kind of new dry process acetylene generator circulating device | |
| CN105481274A (en) | Water processing device and method for household garbage incineration fly ash | |
| CN101746910B (en) | PMIDA wastewater treatment method | |
| CN112723687A (en) | Sludge treatment system | |
| CN211170517U (en) | Hydrogen plasma coal-to-acetylene pulverized coal storage system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170524 |
|
| RJ01 | Rejection of invention patent application after publication |