Classifications

• • 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
  • C02F1/28—Treatment of water, waste water, or sewage by sorption
  • C02F1/286—Treatment of water, waste water, or sewage by sorption using natural organic sorbents or derivatives thereof
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
  • B01D17/02—Separation of non-miscible liquids
  • B01D17/0202—Separation of non-miscible liquids by ab- or adsorption
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
  • B01D47/06—Spray cleaning
• • 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

Definitions

• the invention relates to a method for binding emulsified resin and tar substances in the circulating water of wet scrubber and wet electrostatic precipitator systems for waste gas occurring in the wood industry.
• the raw wood contains a lot of resin (e.g. pine) and is dried at high temperatures (600-800 ° C), besides the cellular water (wood moisture) also a lot of water vapor-volatile resin, tar and fatty acids are stripped out. These substances are still present as gases in the dryer exhaust air at 120 ° C. In the subsequent cooling to the dew point of 50-70 ° C., these substances condense out as aerosols ("blue haze") and can therefore first be deposited as a tar-like coating on the precipitation surfaces of the wet electrostatic precipitator and subsequently washed off with circulating water from there .
• resin e.g. pine
• tar and fatty acids are stripped out.
• the invention aims to provide a method and a plant with which these tar substances are bound by adsorption and can be separated.
• the method according to the invention has the features that into the circulating water Wood dust is metered, which receives the emulsified substances adsorptively, and in that this wood dust is removed from the water circulation ⁇ removed and sedimented.
• a wood dust amount of 100-800% of the original raw gas dust load is preferably additionally added.
• the wood dust is advantageously metered into the exhaust gas fed to the wet washer and wet electrostatic filter system.
• the sediment obtained can either be recirculated in a dryer or burned with other wood waste in a boiler.
• the optimum substance for carrying out the method according to the invention was found to be the grinding dust accumulating in large quantities in the chipboard industry. This occurs with surface smoothing in grinding machines. Wood sanding dust has good properties because its affinity for resin and tar is good, whereby the dust turns dark. The sanding dust also has a corresponding fineness and thus a large surface. In addition, the loaded, wetted grinding dust sediments well.
• the residual product can be disposed of in the form of dewatered sediment either by incineration or in the raw product itself or in a composting facility. It has proven particularly advantageous that a substance is used which corresponds to the natural raw material wood.
• the grinding dust can be added in the course of the method according to the invention into the raw gas line, into the washer, directly into the circulating water or into the return water line of the sludge discharge device.
• the wood dust feed device preferably flows into the wetting device of the exhaust gas feed line via a blowing device.
• the sludge discharge device has a sludge pump and a decanter centrifuge connected downstream thereof, which is connected to the container via a water line.
• the exhaust gas or the exhaust air of a wood drying system (not shown) in a raw gas line 1 is fed via a prewetting device 2 arranged in this to the lower end of a vertical container 3 of the wet washer and wet electrostatic filter system via an inlet 3 '.
• the gas flows upward in the container 3 via a washer device 4 and is cooled to the dew point of 60-70 ° C.
• the condensing aerosols are ionized in a wet electric honeycomb arrangement 5 connected downstream in the flow direction of the gas, to which an electrical high voltage is applied by means of a high voltage unit 6, and are wet ionized in a wet electric filter 7 connected downstream of the honeycomb arrangement 5 or droplet separator.
• the gas leaves the column 3 at the top through an outlet 3 "as a clean gas.
• the residues formed in the container 3 are discharged at the lowest container end as sludge via a sludge pump 7 and a decanter centrifuge 8, which is connected to the container 3 via a water pipe 8 ', and deposited as sediment S.
• the washing water is conveyed up in a circuit, partly via a circuit pump 9 to the scrubber and honeycomb rinse, and partly via a pre-wetting pump 10 to the pre-wetting device 2.
• a wood dust feed device 11 is provided in the area of the raw gas line 1, which has a wood dust silo 12 with a discharge screw 12 'and a ventilator 13 which sprays the wood dust, preferably wood sanding dust, into the pre-wetting device 1.
• the wood dust blown into the pre-wetted raw gas is introduced into the container 3 by the raw gas and in this way reaches the washing water circuit.
• the metering of the wood dust can be regulated according to the respective operating needs via the silo discharge screw 12 '.
• the exemplary embodiment described can be modified within the scope of the general inventive concept.
• the wood dust can thus be added directly into the container 3, into the wash water circuit or into the return water line of the sludge discharge device instead of into the raw gas.

Landscapes

• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Water Supply & Treatment (AREA)
• Organic Chemistry (AREA)
• Life Sciences & Earth Sciences (AREA)
• Hydrology & Water Resources (AREA)
• Engineering & Computer Science (AREA)
• Environmental & Geological Engineering (AREA)
• Physics & Mathematics (AREA)
• Thermal Sciences (AREA)
• Separation Of Particles Using Liquids (AREA)
• Processing Of Solid Wastes (AREA)
• Electrostatic Separation (AREA)
• Manufacture Of Macromolecular Shaped Articles (AREA)
• Adhesives Or Adhesive Processes (AREA)
• Filtering Materials (AREA)

Applications Claiming Priority (3)

Publications (1)

Family

ID=3479124

Family Applications (1)

Country Status (9)

Families Citing this family (10)

Family Cites Families (15)

• 1996
  • 1996-01-02 AT AT0000696A patent/AT402801B/de not_active IP Right Cessation
  • 1996-06-28 US US08/673,363 patent/US5762662A/en not_active Expired - Fee Related
  • 1996-12-12 WO PCT/AT1996/000245 patent/WO1997024293A1/de not_active Ceased
  • 1996-12-12 CZ CZ972613A patent/CZ261397A3/cs unknown
  • 1996-12-12 EP EP96942167A patent/EP0812304A1/de not_active Withdrawn
  • 1996-12-12 CA CA002214149A patent/CA2214149A1/en not_active Abandoned
  • 1996-12-12 AU AU11318/97A patent/AU1131897A/en not_active Abandoned
  • 1996-12-12 PL PL96322050A patent/PL322050A1/xx unknown
• 1997
  • 1997-08-26 NO NO973920A patent/NO973920D0/no unknown
• 1998
  • 1998-04-08 US US09/056,772 patent/US5897689A/en not_active Expired - Lifetime

Non-Patent Citations (1)

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