CN1413927A - Technology and equipment for purifying process water - Google Patents
Technology and equipment for purifying process water Download PDFInfo
- Publication number
- CN1413927A CN1413927A CN 02107400 CN02107400A CN1413927A CN 1413927 A CN1413927 A CN 1413927A CN 02107400 CN02107400 CN 02107400 CN 02107400 A CN02107400 A CN 02107400A CN 1413927 A CN1413927 A CN 1413927A
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- CN
- China
- Prior art keywords
- water
- container
- pieces
- process water
- smashing
- 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.)
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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
- C10J3/02—Fixed-bed gasification of lump fuel
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/18—Nature of the water, waste water, sewage or sludge to be treated from the purification of gaseous effluents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Processing Of Solid Wastes (AREA)
- Filtration Of Liquid (AREA)
- Treatment Of Sludge (AREA)
Abstract
The invention relates to a method and plant for treatment of process water generated when colling and cleaning the inborn gas, in a process of gasifying solid carbon bearing wastes according to a fixed bed pressured gasification and a plag bath gasification. The process water is generated in the form of mixture of thick tar/tar oil/phenol water from two parallel independent back-flush filters fed by twin pipes from a common supply, wherein only one filter operates at all products to be filtered in each case. In the back-flush filter system, residues from each filter are discharged to a pounding container connected with a low-pressure gas system and suspended and diluted by rising water and agitator. Heavy particles e.g. metal or stone collect at the bottom by gravity sedimentation. The stamped residues from filters are smashed, one shunt of which return to the pounding container to raise the eddy current degree of flow along the direction of tangent, the other shunt of which return to process water before filtration stage. And then the process water is further treated by known method. An outstanding feature of the invention is that there is no gaseous matter aggravating the environment burden discharging to the atmosphere.
Description
The present invention relates to the process water that produces when bathing cooling in the technology of gasification (Schlackebadvergasung) solid carbon waste material and cleaning the gas that generates by fixed bed pressure gasification and slag.To this, the gasification of solid carbon waste material can be sneaked into or not sneak into coal and be carried out.The process water that produces in the technology of cooling and cleaning above-mentioned gas contains solid and crosses coarse particles; it does not gasify or partial gasification; discharge with air-flow, and hinder the technology water purification and the aftertreatment of by product, particularly tar-oil-solid particle mixture of in technology, producing.
At present, be used to purify in cooling and to clean the prior art situation of reality of the process water that produces when bathing the gas that the principle of gasification solid carbon waste material generates according to fixed bed pressure gasification and slag as follows:
Continuously the thick tar-tar-phenol water that produces is tar-oil-solid mixture and clear water by the gravity resolution separations in the waste scavenging system of sealing.Then tar-oil-solid mixture is introduced fixed bed gasifiers, entrained flow gasifier (Flugstromvergaser) or slag are bathed in the gasifier, are used at this.The prerequisite of these technologies is that the solid ingredient in tar-oil-solid mixture should have certain particle size distribution, and promptly solid ingredient must not contain the coarse fodder greater than 15mm.At present, the product component of choosing this obstruction is before the processing step gravity sedimentation, finishes by the filtration stage that be arranged in parallel in the thick tar-tar-phenol current of decompression.Here, but with the sieve basket strainer (Siebkorbfilter) of two mutual feed all size of particles are isolated greater than the impurity of 10mm or 15mm.According to the size of particles of the maximum of technical needs, the R-joining filter apparatus (Kantenspaltfilteranlage) of connecting a filter cartridge that has different apertures subsequently is possible.In two filtration processs, the strainer residue is discharged in the atmosphere through decompression technology.
Aspect the problem that exists, proved following point :-in each decompression technology by strainer residue a large amount of emission gases state materials in atmosphere, and the operator to the other work of strainer brings pollution,-the working conditions of complexity by taking the operator that health preventive measures (rubber suit and face protection) bring,-owing to lack the very disadvantageous transportation character of automatization possibility and residue, (dispensing in the total mud aftertreatment outside strainer, be transported in the transport container and transhipment etc.) all need spend a large amount of hand labours outward,-owing on filter surfaces, continue to form the water-borne sediments of fine particle component, being created in quantitatively of strainer filter cake increased sharply, and deposit the centre of-strainer residue, transportation and refuse are got rid of needs a large amount of expenses.
By known a kind of technology that is used for refuse gasification in the document, particle and/or aerosol filter are installed in gas purification apparatus technology in view of the above according to DE 4325689A1.But the material that filters out is not handled and is returned and introduces waste water stream, but introduces in degassing canal and/or the high-temperature reactor in refuse gasification technology, and/or introduces in the water-purification plant mud storage tank.Use about the material that filters out is not introduced.
The discharging of filtrate in atmosphere adopted in one of path of described filtrate at least, and the shortcoming of having mentioned above other thus also must have at this.
Purpose of the present invention and task are, seek a kind of gasifying process for solid carbon raw material, the functional safety that in suitable device, is used for thick tar-tar-phenol water filtration, there is not discharging, cost is favourable, solution that yet can licensed-in technology does not stay any residue that technology is had negative impact thus.
By the solution of this task of the present invention is that the strainer that backwashes (Rueckspuelfilter) of two automatic operations parallel to each other by connecting thick tar-tar-phenol waterpipe is finished.For connecting two strainers that backwash, thick tar-tar-phenol waterpipe separates before filter apparatus.The strainer that backwashes that use has a plurality of punching cylinder fuses (Lochtrommeleinsaetz) and is close to the wiper of punching cylinder outside.Be the filter rinsed element, built-in punching cylinder rotates by the electro-motor on the lid that is arranged on filter head housings.So just can wipe adherent coarse fodder on the strainer.For isolate thick component in advance from thick tar-tar-phenol water, filter housing has a base channel that is designed to taper, and in the bottom, logistics is along tangentially flowing through this groove.
With product the checker of the feed of strainer is depended on that the pressure-losses on filter cartridge that records carries out, it is by importing and deriving ducted regulation and control accessory and realize.When pressure difference on strainer raises, after strainer substitutes, finish automatic developing technique by wash-down water or filtrate, thus the strainer residue is transported to be installed in the strainer below smash to pieces in the container and the filter rinsed fuse.
This container is smashed container (Anmaischgefae β) to pieces as the strainer filter cake of discharging, and agitator is installed.For guaranteeing the hydraulic pressure transportation, in filtrate, sneak into wash-down water by the outflow sleeve pipe of container.Agitator and wash-down water task together is the sedimentary fines of kicking up, and keeps the space of discharging the parts top like this and gives high-density coarse fodder (particularly metal component).The discharge of this coarse fodder is not undertaken by the lock of available wash-down water, nitrogen or steam flush with having discharging.Enter in the sewage lagoon (Slopbehaelter) under nitrogen or steam admission impact from the residual liquid in the lock.
Not only smash container to pieces, and sewage lagoon also is communicated with the low pressure gas system to breathe (Atmung).
Smash container to pieces and be designed to taper for avoiding crust to form (Wandbildung) in the bottom, in addition, its acquisition is close to external heated.
From smash container to pieces, one is taken away this product of smashing to pieces by the combination that repeats to be provided with, be made up of precomminution device and wet-milling millstone by the sleeve pipe that the face down bonding at tapered section connects, and behind disintegrating process, along tangentially above this sleeve pipe, being pumped to (circulation) in the container once more.The maximum size of particles that allows in the technology current is depended in the selection of precomminution device and wet-milling millstone.
In the circulation loop after the wet crushing mill, depend on the liquid level of smashing to pieces in the container, two anastomosing technology water pumps of the mode that can select take out the product of handling, and are back to before filtration stage in the technology current.These pumps have one and are furnished with the driving that revolution is regulated, and this revolution is regulated and made and can react to the work output that changes in the developing technique according to the liquid level of container.
For needn't the interrupt operation process under the out of order situation of filter apparatus, this equipment has by incorporate sieve basket strainer realizes the possibility that detours.The discharge of strainer residue is by backwashing with filtrate, or supplies with wash-down water and carry out, and pre-treatment in the device that need not in the technology current, to be provided with in the strainer upstream.
The advantage of this novel process :-no gaseous substance is discharged in the atmosphere-and do not need the centre of strainer residue to deposit, the expense of transportation and waste treatment, because the strainer filter cake is handled in closed system, and then be back in the technology current,-concerning the operator, there is not a complicated working conditions, because needn't take the health preventive measures, the automatic operation of-filter for installation, there is not hand labour consumption whereby,-pass through strainer, the repeating of pulverizer and transferpump is provided with, and has high equipment controllability.
The present invention will further set forth by embodiment by schema 1.
What produce in fixed bed pressure gasification technology is up to 250m
3Thick tar-the tar of the mixed flow of/h-phenol water 1 flows into behind decompression phase in thick tar-tar-phenol water-reservoir 2, flows to the filter apparatus of the strainer 4 that backwashes that has alternation by dust-thick tar pump 3 at this under 3.5 to 4.5 crust working pressures.Tripping device is designed to respectively to have in the shell form of the sieving drum filter (Siebtrommelfilter) of three fuses.The diameter of sieve aperture is 10mm.The switching point of strainer conversion be according to the technology water yield and the pressure difference on the strainer be 0.2 and 0.3 the crust between, can choose at random by device operator by the setting of rated value.Then, cross filterable thick tar-tar-phenol water (filtrate) 5 and further import to the operation stage of gravity separation.
After the strainer conversion, finish automatic flushing process by wash-down water 15 or filtrate 5, what strainer residue 6 was transported to that the strainer below installs thus smashs to pieces in the container 7 and the filter rinsed fuse.This container is used for the washing of carrying out subsequently and exports the strainer residue of smashing to pieces as susceptor.Be connected with in the conical vessel bottom by each twin shaft coarse fodder pulverizer 10 and two combinations that repetition can move that wet-milling millstone 11 is formed for this reason.This installations are with about 20m
3The volumetric flow rate of/h is extracted the product of smashing to pieces 9 continuously from container out, and is input to columned container top again after by pulverizer, continues upset suspension thus.The coarse fodder component of together carrying thus, changes size of particles into less than 10mm in pulverizer.In circulation loop 12,, also take out shunting 14, and it is imported in thick tar-tar-phenol water-reservoir 2 with the pump 13 that transports that can select mode switch according to tank fill level.The driving of these pumps is furnished with the revolution regulation and control, and it is complementary transmission power and the variation of smashing the liquid level in the container 7 to pieces.
For preventing that pulverizer and transferpump are subjected to the wearing and tearing or the damage of the coarse fodder of high rigidity (metal part, stone etc.), this external separation of smashing these components in the container to pieces is undertaken by sedimentation.For this reason, this container has an agitator 8, and it keeps lighter solid particulate to be kept in motion at the tip of container cone, makes that so heavier solid particulate preferentially deposits near container relief outlet sleeve pipe.The fractionated effect is played in the supply of the wash-down water 15 that is provided with in same zone because wherein lighter particle suspended once more, have only the coarse fodder that especially definitely weighs son stay container outlet.This discharge of once carrying out half a year of sedimentary solid particulate in the container cone is to be undertaken by the manual coarse fodder lock 17 of settling 16 below being arranged in of discharging.The sieve plate that it is 10mm that this lock has an aperture in inside is to hold back thick particle.Unnecessary water and the less son of transporting together 18 can be back to during process water fills, and bigger component is retained on the sieve.With backwash strainer 4 independently of each other, install promising deal with failure condition, have an extra sieve basket strainer 19 of strainer residue 20 being delivered to the vent line in thick tar-tar-phenol water-reservoir 2.
Icon list
1 thick tar-tar-phenol water (Dickteer-Teeroel-Phenolwasser)
2 thick tar-tar-phenol water-reservoir
3 dust-thick tar pump
4 strainers that backwash
5 cross filterable thick tar-tar-phenol water (solution)
6 strainer residues
7 smash container to pieces
8 agitators
9 products of smashing to pieces
10 twin shaft coarse fodder pulverizers
11 wet-milling millstones
12 circulation loops
13 transferpumps
14 shuntings
15 wash-down waters
16 settlings
17 coarse fodder locks
18 unnecessary water and than small-particle
19 sieve basket strainers
20 strainer residues sieve strainer
Claims (2)
1. the purifying process water method that is used for process water, described process water is in bathe gasifying process gasification solid carbon waste material technology according to fixed bed pressure gasification and slag, when cooling off and clean the gas that wherein generates, produce, it has the following step :-will be parallel at two by thick tar-tar-phenol water that thick tar-tar-phenol water-reservoir takes out, independently, wherein have only under every kind of situation in the filter system that backwashes and filter with the product operation to be filtered of all amounts, rotatable punching cylinder fuse and fixed wiper that-two parallel strainers that backwash are installed by inside come self-stip,-by the bottom that the thick component of product to be filtered is separated to filter housing along shoving of tangent line,-according to the pressure-losses on filter cartridge, automatically the feed that substitutes the filter system that backwashes, subsequently to its flushing and cleaning,-the strainer residue of two strainers that backwash is transported to smashing to pieces in the container of connection lp system, here continuing under the stirring, smash to pieces by the feeding wash-down water,-the strainer residue of feeding is separated into highdensity coarse fodder (metal in smashing the tapered lower portion of container to pieces, stone etc.), it is collected in the drain sleeve of smashing container to pieces, and the fines that is retained in the state of kicking up by wash-down water and agitator,-from the drain sleeve of smashing container to pieces, discharge highdensity coarse fodder off and on to the coarse fodder lock,-aspirate out the product of smashing to pieces He kick up in the container by smashing to pieces, then it is crushed to desirable size of particles in one or more crushing process, and behind shredding stage, the part of product is back to smashing to pieces in the container above the suction point,-according to the liquid level of smashing container to pieces, another part of product behind the crushing process is taken out, and be back in the preceding technology current of filtration stage,-when filtration stage is out of order, available additional sieve basket strainer is realized the possibility that process water detours ,-process water of having removed coarse fodder is therebetween further handled by already known processes.
2. be used to implement according to the method for claim 1, the purifying process water device of water is used to plant, described process water is in bathe the technology gasification solid carbon waste material technology of gasification according to fixed bed pressure gasification and slag, when the gas of cooling and cleaning generation, produce, this device is along having following setting on the flow direction of process water :-installation separates with atmosphere, the technology water yield for total generation is enough big, thick tar-tar-phenol water-the reservoir that has the transferpump of subsequent installation, two of-installations are parallel, alternately also turn round automatically, conical lower portion is arranged, each installs a plurality of rotating in inside, the outside is glued with the punching cylinder fuse of wiper, wherein the aperture of punching cylinder is 10mm, also has the strainer that backwashes that other is used for the equipment of process water and wash-down water importing and derivation,-install to receive the strainer residue of the strainer that backwashes, container bottom with taper, be arranged in the agitator of tapered lower portion and comprise and be used to the product round-robin smashing to pieces and pulverize, be used to import and derive product equipment smash container to pieces,-be installed in the precomminution and the broken equipment of wet-milling that are used for stamp product in the described circulation, comprise conveying, import and derivation equipment,-below smashing container to pieces, install with atmosphere and separate, have and return unnecessary water and than the coarse fodder lock of the device of small-particle,-in the coarse fodder lock, installation is used to hold back coarse fodder, has sieve annex to the desirable aperture of technology,-install additional, screen filter independently, it has independently, be used to link the equipment of system so far.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE10152985.6 | 2001-10-26 | ||
| DE2001152985 DE10152985A1 (en) | 2001-10-26 | 2001-10-26 | Process to concentrate thick tar/tar oil/phenol water involves filtration by two automated parallel back-flush filters |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1413927A true CN1413927A (en) | 2003-04-30 |
| CN1173014C CN1173014C (en) | 2004-10-27 |
Family
ID=7703864
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB021074003A Expired - Fee Related CN1173014C (en) | 2001-10-26 | 2002-03-21 | Technology and equipment for purifying process water |
Country Status (4)
| Country | Link |
|---|---|
| CN (1) | CN1173014C (en) |
| CZ (1) | CZ20023492A3 (en) |
| DE (1) | DE10152985A1 (en) |
| ZA (1) | ZA200203809B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109072100A (en) * | 2016-05-16 | 2018-12-21 | 三菱日立电力系统株式会社 | Clinker discharge system, gasification furnace and slag filtration method |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CZ299890B6 (en) * | 2005-02-18 | 2008-12-29 | Müller@Rudolf | Multistage absorption separator |
| US7896955B2 (en) | 2007-11-12 | 2011-03-01 | General Electric Company | Low temperature solids removal system for gasification |
| US9051517B2 (en) | 2011-02-01 | 2015-06-09 | Sasol Technology (Proprietary) Limited | Tar recovery from gasification of a carbonaceous feedstock |
-
2001
- 2001-10-26 DE DE2001152985 patent/DE10152985A1/en not_active Withdrawn
-
2002
- 2002-03-21 CN CNB021074003A patent/CN1173014C/en not_active Expired - Fee Related
- 2002-05-14 ZA ZA200203809A patent/ZA200203809B/en unknown
- 2002-10-21 CZ CZ20023492A patent/CZ20023492A3/en unknown
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109072100A (en) * | 2016-05-16 | 2018-12-21 | 三菱日立电力系统株式会社 | Clinker discharge system, gasification furnace and slag filtration method |
| US11292976B2 (en) | 2016-05-16 | 2022-04-05 | Mitsubishi Power, Ltd. | Slag discharge system, gasifier, and slag filtration method |
Also Published As
| Publication number | Publication date |
|---|---|
| DE10152985A1 (en) | 2003-05-15 |
| CZ20023492A3 (en) | 2004-02-18 |
| ZA200203809B (en) | 2002-07-30 |
| CN1173014C (en) | 2004-10-27 |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
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Owner name: SUSTEC SCHWARZE PUMPE GMBH Free format text: FORMER OWNER: MATERIAL REUSE CENTER SCHVARTZ PENBO GMBH Effective date: 20060707 |
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Effective date of registration: 20060707 Address after: The Federal Republic of Germany the rewa porcelain Patentee after: Sustec Schwarze Pumpe GmbH Address before: The Federal Republic of Germany the rewa porcelain Patentee before: Material Reuse Center Schvartz Penbo GmbH |
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