KR890003127B1 - Process for decolorising of waste water - Google Patents
Process for decolorising of waste water Download PDFInfo
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- KR890003127B1 KR890003127B1 KR1019860011457A KR860011457A KR890003127B1 KR 890003127 B1 KR890003127 B1 KR 890003127B1 KR 1019860011457 A KR1019860011457 A KR 1019860011457A KR 860011457 A KR860011457 A KR 860011457A KR 890003127 B1 KR890003127 B1 KR 890003127B1
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- coke
- waste water
- ton
- decolorization
- chromaticity
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- 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
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S210/00—Liquid purification or separation
- Y10S210/902—Materials removed
- Y10S210/917—Color
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
- Fertilizers (AREA)
Abstract
Description
제1도는 착색방류수/침전지분코크스의 값에 따른 방류수의 색도 및 색도제거율을 나타낸그래프.1 is a graph showing the chromaticity and chromaticity removal rate of the discharged water according to the value of the colored discharged water / sedimentation coke.
제2도는 코크스 제조공장 폐수처리공정도.2 is a coke manufacturing plant wastewater treatment process.
본 발명은 탈색방법 특히, 코크스 제조공장착색 방류수의 탈색 방법에 관한 것이다.The present invention relates to a bleaching method, in particular a bleaching method of the coke manufacturing plant coloring discharged water.
통상, 코크스제조공장에서 석탄(유연탄)을 고온(1200-1350℃)으로 건류(16-19시간)하여 코크스를 제조할때 석탄에 부착된 수분과 중, 축합반응에 의하여 생성된 수분이 폐수로 발생하게 되며 이를 활성오니법 및 감청법(제 2 도참조)에 의해 오염물질인 페놀, 시안등을 제거하고 방류하나 황갈색 또는 황색으로 착색되어 있기때문에 미관상 공해요인이 되므로 방류수의 탈색이 요구되어왔다.In general, when coke is manufactured by coking coal (briquette) at high temperature (1200-1350 ° C.) in a coke manufacturing plant to produce coke, the water attached to the coal and the water generated by the condensation reaction are discharged into the wastewater. This is caused by the removal of pollutants such as phenol and cyan by activating sludge method and tapping method (see Fig. 2). .
종래 코크스제조공장 폐수의 탈색방법으로는 활성탄에 의한 흡착법만이 알려져 있으며, 일반적인 염색공장 폐수의 탈색방법으로는 염소, 차아염소산염, 오존등에 의한 산화탈색법, 철, 아연, 황화수소등에 의한 환원탈색법과 황산알루미늄, 제 1 철 또는 제 2 철 염, 고분자응집제등에 의한 응집탈색법에 알려져 있으나 흡착법 이외의 타방법은 코크스 제조공장폐수의 탈색에는 효과가 없다.Conventionally, only the adsorption method using activated carbon is known as the decolorization method of wastewater from coke manufacturing plant. As the decolorization method of general wastewater from dyeing plant, oxidation decolorization method using chlorine, hypochlorite, ozone, etc., reduction decolorization method using iron, zinc, hydrogen sulfide, etc. Although it is known for the coagulation and decolorization by aluminum sulfate, ferrous or ferric salts, and polymer coagulants, other methods other than adsorption are not effective for the decolorization of the coke plant wastewater.
한편, 활성탄 흡착법은 활성탄이 니탄, 아탄등을 원료로하여 염화아연, 인산, 황산등으로 부활 제조되거나, 목탄(야자껍질)등을 원료로하여 500-600℃로 탄화하고 수증기로 부활, 제조되므로 제조 및 재생비용이 많이 들고, 전기공용극(Total porevolume)이 적기때문에 탈색효과에 한계가 있는 문제점이 있다.On the other hand, activated carbon adsorption method uses activated carbon as nitride, ethane, etc. as a raw material to revitalize zinc chloride, phosphoric acid, sulfuric acid, etc., or charcoal (palm shell) etc. as carbon raw material at 500-600 ℃ and revive it with steam. There is a problem in that the manufacturing and regeneration costs are high, and because the total porevolume is small, the discoloration effect is limited.
상기문제점은 해결하기위하여, 본 발명은 탈색효율이 우수하고 경제적인 코크스 제조공장착색 방류수의 탈색방법을 제공하고자 하는 것이다.In order to solve the above problems, the present invention is to provide a method of decolorization of the colored effluent of the coke manufacturing plant excellent in decolorization efficiency and economical.
이하 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail.
본 발명은, 코크스 제조공장 착색방류수의 탈색방법에 있어서, 착색 방류수(ton)/첨전지 분코크스(ton)값이 7.5이하가 되도록 침전지 분코크스를 탈색제로 사용하여 탈색함을 특징으로하는 코크스 제조공장 착색방류수의 탈색방법에 관한것이다.In the present invention, in the method for decolorization of the colored effluent in the coke production plant, the coke is characterized in that the precipitated powdered coke is decolorized so that the color discharged water (ton) / battery powder coke (ton) value is 7.5 or less. It is about the discoloration method of factory colored discharge water.
상기에서, 착색방류수(ton)/침전지 분코크스(ton)의 값이 7.5이상인 경우 침전지 분코크스의 흡착용량이 저하되므로 7.5이하가 바람직하다.In the above, when the value of the colored discharge water (ton) / settling powder coke (ton) is 7.5 or more, the adsorption capacity of the sedimentation basin coke is lowered is preferably 7.5 or less.
본 발명의 침전지 분코크스는 일반 분코크스 및 활성탄보다 입도가 미세하고 전기공용적이 크기때문에 탈색효율이 클뿐만 아니라, 방류수 처리전과 처리후의 발열량이 변화하지 않으므로, 철광석 소결용등의 연료로 재사용될 수 있다.The sedimentation basin coke of the present invention has a higher particle dissipation efficiency because of finer particle size and larger electric common volume than ordinary coke and activated carbon, and the calorific value does not change before and after effluent treatment, and thus can be reused as a fuel for iron ore sintering. have.
상기와같이 구성된 본 발명은 코크스 제조공장에서 방류되는 방류수중의 색도를 경계적이고 효과적으로 제거할 수 있는 현저한 효과를 제공한다.The present invention configured as described above provides a remarkable effect that can remove the chromaticity in the discharged water discharged from the coke manufacturing plant boundary and effectively.
이하 실시예를 통하여 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail through examples.
[실시예 1]Example 1
종래방법과 본 발명을 비교하기 위하여 3㎜ 이하의 일반 분코크스, 12-30mesh의 활 성탄, 그리고 3㎜ 이하의 본 발명의 침전지분코크스 200g을 내경 3㎝, 길이 58㎝의 아크릴 흡착탑에 각각 충진하여 코크스 제조공장원페수와 방류수 500ml을 흡착법으로 각각 처리하였으며, PAA, Al2(SO4)3및 NaOCl을 각각 50-200mg/l의 농도를 코크스 제조공장 원폐수와 방류수에 각각 주입하여 분당 150회전수로 조절된 자테스터에서 1시간동안 응집법, 산화법으로 각각처리하였다.In order to compare the present invention with the conventional method, the powdered coke of 3 mm or less, activated carbon of 12-30 mesh, and 200 g of precipitated branch coke of the present invention of 3 mm or less are filled in an acrylic adsorption column having an inner diameter of 3 cm and a length of 58 cm, respectively. Coke manufacturing plant wastewater and 500ml of effluent were treated by adsorption method, respectively. PAA, Al 2 (SO 4 ) 3 and NaOCl were injected into coke plant wastewater and effluent respectively at concentrations of 50-200mg / l. In the tester controlled by the rotation speed, it was treated for 1 hour by flocculation and oxidation.
상기처리후에 원폐수 및 방류수의 탁도, 색도 및 색도제거율을 측정하여 표1에 나타내었다.After the treatment, the turbidity, chromaticity, and chromaticity removal rate of the raw wastewater and the effluent were measured and shown in Table 1.
[표 1]TABLE 1
* + : 색도가 증가되었음을 의미함.* +: Chromaticity is increased.
상기 표1에서와 같이 고분자응집제(PAA)및 Al2(SO4)3에 의한 응집탈색법은 색도제거율이 낮으며 NaOCl에 의한 산화 탈색법은 시안을 제거하기 위하여 주입된 과잉의 염화 제 2 철 중의 철이온과 NaOCl중의 산소와 반응하여 색도가 증가됨을 알 수 있다.As shown in Table 1, the coagulation bleaching method using the polymer coagulant (PAA) and Al 2 (SO 4 ) 3 has a low color removal rate, and the oxidative bleaching method using NaOCl is used to remove the excess ferric chloride. It can be seen that the chromaticity is increased by reacting with iron ions and oxygen in NaOCl.
[실시예 2]Example 2
본 발명의 침전지 분코크스에 의한 탈색 용량을 측정하기위하여 방류수 200, 500, 1000, 1500 및 2500ml를 본 발명의 침전지 분코크스 200g이 충진된 내경 3㎝, 길이 58㎝의 아크릴 흡착탑에서 연속적으로 흡착탈색처리 하였다.In order to measure the decolorization capacity by the sedimentation powder coke of the present invention, 200, 500, 1000, 1500 and 2500 ml of effluent were continuously adsorbed and decolorized in an acrylic adsorption column having an inner diameter of 3 cm and a length of 58 cm filled with 200 g of the sedimentation powder coke of the present invention. Processed.
상기 방류수는 처리전의 색도가 183이고 황갈색을 갖는다.The discharged water had a chromaticity of 183 and a yellowish brown color before treatment.
상기처리후 본 발명예 및 비교예에 대한 색도, 색도 제거율(%) 및 색을 측정하여 그 결과치를 표2 및 보다 명확히 설명하기 위하여 제 1 도에 나타내었다.After the above treatment, the chromaticity, chromaticity removal rate (%), and color of the inventive examples and the comparative examples were measured, and the results are shown in Table 2 and in order to explain more clearly.
[표 2]TABLE 2
상기에서 알수 있는 바와같이, 본 발명은 코크스 제조공장 착색방류수를 경제적이고 탈색효율이 우수한 침전지 분코크스를 사용하여 탈색하므로 공해방지, 자원활용 및 원가절감을 기하는 효과가 있다.As can be seen from the above, the present invention has the effect of preventing pollution, resource utilization and cost reduction because the color of the discharged coke manufacturing plant using the sedimentation basin coke is economical and excellent decolorization efficiency.
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KR1019860011457A KR890003127B1 (en) | 1986-12-29 | 1986-12-29 | Process for decolorising of waste water |
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KR1019860011457A KR890003127B1 (en) | 1986-12-29 | 1986-12-29 | Process for decolorising of waste water |
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KR890003127B1 true KR890003127B1 (en) | 1989-08-23 |
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