Purification method of odor waste gas produced by high-temperature dewatering of sludge

A high temperature, exhaust gas technology, applied in chemical instruments and methods, separation methods, air quality improvement, etc., can solve the problems of low deodorization efficiency, increased energy consumption, difficulty in maintaining activity, etc., achieve good low temperature survival performance, increase wastewater treatment Burden, low-cost odor treatment effect

Active Publication Date: 2011-09-14
广州市越堡水泥有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0013] 3. The use of normal temperature biological method must reduce the exhaust gas temperature to within 15 ~ 37 ℃, so as to maintain the activity of microorganisms, while the temperature of the tail gas discharged from the sludge drying equipment is still 120 ℃, the microorganisms cannot survive at room temperature, and cooling measures should be taken It will greatly increase energy consumption; and the humidity content in the exhaust gas is relatively large, about 18%. When the temperature of the exhaust gas is lower than 60°C, condensed water will be precipitated, and when the temperature drops below 37°C, a large amount of condensed water will be precipitated, forming secondary Pollution
[0014] 4. Use wet desulfurization to remove SO 2 The final waste gas temperature is still 60-70°C, and the room-temperature microorganisms in the room-temperature biological method are still difficult to maintain activity, and the deodorization efficiency is extremely low

Method used

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  • Purification method of odor waste gas produced by high-temperature dewatering of sludge
  • Purification method of odor waste gas produced by high-temperature dewatering of sludge
  • Purification method of odor waste gas produced by high-temperature dewatering of sludge

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Embodiment 1

[0040] The method for purifying the malodorous waste gas produced by high-temperature dehydration of sludge described in this embodiment comprises the following steps:

[0041] (1) Limestone-gypsum desulfurization system to remove SO 2 ;Limestone-gypsum desulfurization system mainly includes absorption tower, limestone slurry circulating spray system, flue system, defogging system, limestone slurry preparation system and gypsum dehydration system;

[0042] The malodorous exhaust gas is sent from the bottom of the absorption tower to the absorption tower through the pressurization of the induced draft fan, and the temperature of the smoke entering the tower is controlled at 110-130°C, and the slurry spray volume is 15L / Nm 3 , the number of demisters is two, and the tower height is 32m. Measure SO in tower exhaust gas 2 Less than 50mg / L, and the temperature of the malodorous exhaust gas is between 55 and 64°C;

[0043] (2) High-temperature biological trickling filter deodoriz...

Embodiment 2

[0053] The method for purifying the malodorous waste gas produced by high-temperature dehydration of sludge described in this embodiment comprises the following steps:

[0054] (1) Limestone-gypsum desulfurization system to remove SO 2 ;Limestone-gypsum desulfurization system includes absorption tower, limestone slurry circulating spray system, flue system, demisting system, limestone slurry preparation system and gypsum dehydration system;

[0055] The malodorous exhaust gas is sent from the bottom of the absorption tower to the absorption tower through the pressurization of the induced draft fan, and the temperature of the smoke entering the tower is controlled at 110-130°C, and the slurry spray volume is 10L / Nm 3 , the number of demisters is two, and the tower height is 29m. Measure SO in tower exhaust gas 2 The concentration is lower than 50mg / L, and the temperature of the malodorous exhaust gas is between 55°C and 64°C; (2) The high-temperature biological trickling filt...

Embodiment 3

[0065] The method for purifying the malodorous waste gas produced by high-temperature dehydration of sludge described in this embodiment comprises the following steps:

[0066] (1) Limestone-gypsum desulfurization system to remove SO 2 ;Limestone-gypsum desulfurization system includes absorption tower, limestone slurry circulating spray system, flue system, demisting system, limestone slurry preparation system and gypsum dehydration system;

[0067] The malodorous exhaust gas is sent from the bottom of the absorption tower to the absorption tower through the pressurization of the induced draft fan, and the temperature of the smoke entering the tower is controlled at 110-130°C, and the slurry spray volume is 15L / Nm 3 , the number of demisters is two, and the tower height is 35m. Measure SO in tower exhaust gas 2 The concentration is lower than 50mg / L, and the temperature of the malodorous exhaust gas is between 55 and 64°C;

[0068](2) High-temperature biological trickling f...

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Abstract

The invention discloses a purification method of odor waste gas produced by high-temperature dewatering of sludge. In the process method, two parts, namely a limestone-gypsum desulfurization system and a high-temperature biological drop-filtering tower deodorizing system, are included, wherein SO2 in the odor waste gas is removed by a desulfurizing tower, and then high-temperature deodorizing thermophilic bacterium groups in biological fillers are used to degrade odor and organic components in the odor waste gas by the biological drop-filtering tower. The innovative combined process has the advantages that the deodorization effect is obvious, and a matched cooling system is not needed, so that a large amount of condensate water is prevented from being dissolved out, the investment is saved, the operating cost is low and no secondary pollution is caused.

Description

technical field [0001] The invention belongs to the technical field of waste gas treatment, and in particular relates to a process method for purifying malodorous waste gas produced by high-temperature dehydration of sludge by using a chemical method combined with a biological method. Background technique [0002] The incineration method is one of the main methods to treat the sludge of the urban sewage plant, and its main process is to dry the sludge first, and then incinerate it. Since the moisture content of raw sludge is above 80%, direct incineration requires a large amount of fuel, which is very uneconomical. Usually, the sludge is dried and dehydrated before incineration, and the volume of the dried sludge will be greatly reduced. The main component of dewatered sludge is carbon organic matter, which has a high calorific value, and then decomposed by incineration can save a lot of fuel. The sludge incineration products only have a small amount of residual inorganic s...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/80B01D53/85B01D53/50B01D53/44
CPCY02A50/20
Inventor 陈文和张小雄邓明佳刘颖成张斌林益晓罗辉刘志强曾钜键
Owner 广州市越堡水泥有限公司
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