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Method for removing flue gas through rosin condensate recovery

A technology for condensed water and flue gas, applied in the direction of separation methods, chemical instruments and methods, grease/oily substances/suspton removal devices, etc., can solve the problems of slow microbial growth cycle, high operating cost, and poor treatment effect, and achieve The processing process is simple, the safety hazard is reduced, and the effect of easy production

Inactive Publication Date: 2016-12-14
广西兴业县新贵松脂厂
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] The distillation process of turpentine processing requires a large amount of condensed water for cooling. However, in conventional processing methods, the condensed water will be discharged through recycling and wastewater treatment. However, the condensed water is relatively clean compared to turpentine wastewater and can be used for recycling. However, due to Condensed water contains a mixture of oil and fat, which is easy to burn. Flue gas is the gas produced by the boiler after combustion. The temperature can reach about 150°C-200°C. The condensed water distilled from turpentine is directly refluxed for water film dust removal, which may cause combustion and cause safety accidents. , and, the flue gas contains a large amount of SO 2 and NO x It will cause great pollution to the environment. Nowadays, industrially remove SO from flue gas 2 and NO x The method of wet limestone is commonly used for removal, but the use of wet lime method has the disadvantages of high equipment operation cost, large floor area, easy scaling and corrosion of equipment, and easy to cause secondary pollution, and some use microbial flora to treat the flue gas SO 2 and NO x However, due to the slow growth cycle of microorganisms and poor treatment effect, there is currently no method to use condensed water distilled from rosin to remove dust from flue gas without causing secondary pollution
Therefore, in the process of recovering flue gas from turpentine distillation condensate, the following problems need to be solved: (1) the condensed water contains grease, which will cause fire and cause a fire when it encounters high temperature; (2) the condensed water cannot effectively remove SO in the flue gas 2 and NO x , the conventional method has a slow treatment effect and occupies a large area, which will cause secondary pollution

Method used

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  • Method for removing flue gas through rosin condensate recovery
  • Method for removing flue gas through rosin condensate recovery

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] 1. Microbial activation:

[0022] (1) The configuration of the medium is according to the following medium ratio:

[0023] A medium configuration: The medium components are mixed and configured according to the following components, 0.3g of K 2 HPO 4 , 0.8 g NH 4 Cl, 1.0g yeast extract, 0.1g CaCl 2 ·H 2 O, 0.02g FeSO 4 ·7H 2 O, 5ml of 60%-70% sodium lactate solution, 800ml of distilled water, the pH value of the culture medium is 6, after the culture medium is prepared, sterilize it with steam at 120°C for 20min;

[0024] B medium configuration: The medium components are mixed and configured according to the following components, 0.5g of CH 3 COONa, 0.1 g KNO 3 , 0.02g K 2 HPO 4 , 0.02g MgCl 2 , 0.01gCaCl 2 , 800ml of distilled water, the pH value of the medium is 7, and the medium is sterilized with steam at 120°C for 20 minutes after the medium is prepared;

[0025] (2) Inoculation activation:

[0026] ① Inoculate the original species of Thiobacillus fer...

Embodiment 2

[0033] 1. Microbial activation:

[0034] (1) The configuration of the medium is according to the following medium ratio:

[0035] A medium configuration: The medium components are mixed and configured according to the following components, 0.6g of K 2 HPO 4 , 1.2 g NH 4 Cl, 1.5g yeast extract, 0.3g CaCl 2 ·H 2 O, 0.04 g FeSO 4 ·7H 2 O, 10ml of 70% sodium lactate solution, 1400ml of distilled water, the pH value of the medium is 8, after the medium is prepared, sterilize it with steam at 130°C for 30min;

[0036] B medium configuration: The medium components are mixed and configured according to the following components, 1.0g of CH 3 COONa, 0.5 g KNO 3 , 0.05g K 2 HPO 4 , 0.05g MgCl 2 , 0.03gCaCl 2 , 1500ml of distilled water, the pH value of the medium is 7.5, and the medium is sterilized with steam at 130°C for 30 minutes after the medium is prepared;

[0037] (2) Inoculation activation:

[0038] ① Inoculate the original species of Thiobacillus ferrooxidans in m...

Embodiment 3

[0045] 1. Microbial activation:

[0046] (1) The configuration of the medium is according to the following medium ratio:

[0047] A medium configuration: The medium components are mixed and configured according to the following components, 0.5g of K 2 HPO 4 , 1.0 g NH 4 Cl, 1.3g yeast extract, 0.2g CaCl 2 ·H 2 O, 0.03g FeSO 4 ·7H 2 0, 8ml of 65% sodium lactate solution, 1000ml of distilled water, the pH value of the medium is 7, after the medium is prepared, sterilize it with steam at 125°C for 25min;

[0048] B medium configuration: The medium components are mixed and configured according to the following components, 0.8g of CH 3 COONa, 0.3 g KNO 3 , 0.04g K 2 HPO 4 , 0.04g MgCl 2 , 0.02gCaCl 2 , 1000ml of distilled water, the pH value of the medium is 7.3, and the medium is sterilized with steam at 125°C for 25 minutes after the medium is prepared;

[0049] (2) Inoculation activation:

[0050] ① Inoculate the original species of Thiobacillus ferrooxidans in cul...

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PUM

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Abstract

The invention belongs to the field of recovering and using rosin condensate, and discloses a method for removing flue gas through rosin condensate recovery. The condensate is recovered for oil water separation, a microorganism solution containing desulfurizing bacteria and denitrifying bacteria is added and serves as circulating absorbing liquid, sulfate ions and nitrate ions in the flue gas absorbing waste water are treated, so that the safety rate of the rosin distillation condensate is increased, SO2 and NOx in the flue gas can be effectively removed, while a conventional method is slow in treatment speed and large in occupied area and causes secondary pollution.

Description

【Technical field】 [0001] The invention relates to the field of recycling turpentine condensed water, in particular to a method for recycling turpentine condensed water and removing smoke. 【Background technique】 [0002] The distillation process of turpentine processing requires a large amount of condensed water for cooling. However, in conventional processing methods, the condensed water will be discharged through recycling and wastewater treatment. However, the condensed water is relatively clean compared to turpentine wastewater and can be used for recycling. However, due to Condensed water contains a mixture of oil and fat, which is easy to burn. Flue gas is the gas produced by the boiler after combustion. The temperature can reach about 150°C-200°C. The condensed water distilled from turpentine is directly refluxed for water film dust removal, which may cause combustion and cause safety accidents. , and, the flue gas contains a large amount of SO 2 and NO x It will cau...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/38C02F1/40B01D53/18B01D53/84B01D53/56B01D53/50
CPCB01D53/18B01D53/502B01D53/56B01D53/84C02F1/38C02F1/40Y02A50/20
Inventor 梁业邦
Owner 广西兴业县新贵松脂厂
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