Deep phosphorous removal method for low-phosphorous water

A deep, crystal seed technology, applied in the field of deep phosphorus removal of secondary treatment effluent and landscape water, can solve the problems of unstable biological phosphorus removal process, high sludge moisture content, complex process flow, etc., to save investment and The effect of running cost, good treatment effect and simple process flow

Inactive Publication Date: 2015-01-28
BEIJING MUNICIPAL RES INST OF ENVIRONMENT PROTECTION
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantage of this method is that the biological phosphorus removal process is unstable, and the final performance is sludge removal and phosphorus removal, which is likely to cause secondary pollution. In addition, phosphorus removal and nitrogen removal are carried out at the same time in most cases. There are contradictions in other aspects, so that the two cannot be balanced
This method can reduce the cost of phosphorus removal and obtain a stable phosphorus removal effect, but there are still disadvantages such as complex process flow, large amount of sludge, high moisture content of sludge, difficult dehydration, and easy to produce secondary pollution.

Method used

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  • Deep phosphorous removal method for low-phosphorous water
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  • Deep phosphorous removal method for low-phosphorous water

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0056] The specific operating parameters are: first-stage fluidized bed reactor: the total effective volume is 3.8L, and 350g of 0.3-0.1mm modified coral sand is put into it. The average influent flow rate is 15.72L / d, the hydraulic retention time is 5.46h, and the aeration rate is 200L / h. Secondary fixed-bed reactor: 4.17kg of modified coral sand of 0.45-1.0mm is input, the sand layer is 12cm high, the effective volume of the sand bed is 3.19L, the average influent flow rate is 16.71L / d, and the hydraulic retention time of the sand layer is 4.58h . The raw water is the secondary treatment effluent of domestic sewage, with an average TP=3.27mg / L. Calcium chloride is the calcium source, in the reactor [Ca 2+ ]=80~150mg / L, adjust the pH in the range of 8.5~10.0 with 0.1M NaOH.

[0057] The operation effect is as follows figure 2 Shown: The total removal rate of the series system is 96.33%. The average influent TP of the primary reactor is 3.27mg / L, the average effluent TP ...

Embodiment 2

[0059] The specific operating parameters are: Secondary fixed bed reactor: input 4.17kg of 2.5-1.0mm modified coral sand, the height of the sand layer is 12cm, the effective volume of the sand bed layer is 3.19L, the average water flow rate is 16.6L / d, the sand layer The hydraulic retention time is 4.63h. The raw water is a landscape water body in a residential area, with an average TP=1.19mg / L. With calcium chloride as calcium source, [Ca 2+ ]=80~150mg / L, adjust the pH in the range of 8.5~10.0 with 0.1M NaOH.

[0060] The operation effect is as follows image 3 Shown: The reactor can run continuously and stably for a long time, and the average removal rate of TP is 97.16% within 50 days of continuous monitoring. The average influent TP of the reactor is 1.19mg / L, the average effluent TP is 0.034mg / L, and the pH of the effluent is always within the range of 8.5 to 7.5, stably reaching the standard limit of surface water category III (lakes and reservoirs TP≤0.05mg / L) value...

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Abstract

The invention discloses a deep phosphorous removal method for low-phosphorous water, belonging to the field of sewage treatment and relating to phosphorous removal applying an HAP crystallization method. The deep phosphorous removal method comprises the following steps: step 1, preparing modified coral sand; sieving natural coral sand and taking the coral sand with the grain diameter being 0.3mm-0.1mm as a raw material for preparing a first-stage fluidized bed reactor crystal seed; taking the coral sand with the grain diameter being more than 0.45mm as a raw material for preparing a second-stage fixed bed reactor crystal seed and modifying to generate hydroxylapitide on the surface; and step 2, enabling the low-phosphorous water to sequentially pass through a first-stage fluidized bed and a second-stage fixed bed and adding an alkali to adjust the pH value to 8.5-10.0; and meanwhile, adding a calcium salt solution and converting Ca<2+>, PO4<3-> and OH<-> in the water into hydroxylapitide to be crystalized on the surface of the coral sand, so as to remove phosphorous in the low-phosphorous water. The deep phosphorous removal method has strong technological controllability, stability in operation, good treatment effect and simple process flow; the investment and operation costs are saved; and filtering materials can be used for recycling phosphorous.

Description

technical field [0001] The invention belongs to the field of sewage treatment and relates to phosphorus removal by using a HAP crystallization method, and is especially suitable for deep phosphorus removal of secondary treatment effluent and landscape water. Background technique [0002] Phosphorus is the most important factor for water eutrophication. The current internationally recognized standard is: when the total nitrogen content in the water body is greater than 0.2mg / L, and the total phosphorus content is greater than 0.02mg / L, the water body will be eutrophic. In natural water bodies such as lakes and estuaries, when the nitrogen content in the water is insufficient, it can be supplemented by some nitrogen-fixing microorganisms, but there is no such supplementary method for phosphorus, and it can only be supplemented by external phosphorus sources. Compared with nitrogen, aquatic algae are more sensitive to phosphorus, so if phosphorus can be controlled at a low leve...

Claims

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Application Information

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IPC IPC(8): C02F9/04
CPCC02F9/00C02F2001/5218C02F2101/105C02F2301/08
Inventor 刘寅杜兵曹建平何然王珊
Owner BEIJING MUNICIPAL RES INST OF ENVIRONMENT PROTECTION
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