CN115571980A - A UASB reactor for treating high-concentration papermaking wastewater - Google Patents
A UASB reactor for treating high-concentration papermaking wastewater Download PDFInfo
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- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 title claims abstract description 31
- 239000002351 wastewater Substances 0.000 title claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 54
- 239000000523 sample Substances 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims 4
- 239000010802 sludge Substances 0.000 abstract description 12
- 239000010865 sewage Substances 0.000 abstract description 7
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 239000008187 granular material Substances 0.000 abstract 4
- 238000000034 method Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
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- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001699 photocatalysis Effects 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000011197 physicochemical method Methods 0.000 description 1
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2846—Anaerobic digestion processes using upflow anaerobic sludge blanket [UASB] reactors
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/26—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof
- C02F2103/28—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof from the paper or cellulose industry
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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
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- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
Description
技术领域technical field
本发明涉及UASB反应器技术领域,特别涉及一种用于处理高浓度造纸废水的UASB反应器。The invention relates to the technical field of UASB reactors, in particular to a UASB reactor for treating high-concentration papermaking wastewater.
背景技术Background technique
制浆造纸废水属于高浓度有机废水,国家对其排放标准要求较为严格。造纸废水成复杂,主要特点为色度较高、COD较高,包含多种其他化学物质。目前,处理造纸废水的技术主要有物理法、化学法、物理化学法、生物法、膜技术和光催化法等。而在众多的处理方法中,厌氧生物处理技术因为具有能耗低、工作负荷高及二次污染小等优点,已成为造纸废水的首选预处理方法。Pulping and papermaking wastewater is a high-concentration organic wastewater, and the country has stricter requirements on its discharge standards. The composition of papermaking wastewater is complex, the main features are high chroma, high COD, and contains a variety of other chemical substances. At present, the technologies for treating papermaking wastewater mainly include physical methods, chemical methods, physicochemical methods, biological methods, membrane technology and photocatalytic methods. Among many treatment methods, anaerobic biological treatment technology has become the preferred pretreatment method for papermaking wastewater because of its advantages of low energy consumption, high workload and low secondary pollution.
本发明基于高浓度有机物废水进入反应层,污水无法和反应层内颗粒污泥充分接触反应,从而导致反应缓慢,去除效率低,水温不均匀,并且在三相分离器上方漂浮中空颗粒污泥等问题,构建了一种厌氧外部循环系统,从而达到强化污染物去除、控制水温恒定、促进新老颗粒污泥更替生长等目的,显著提高了去除效率,为缓解后续生化反应工作负荷提供保障。The present invention is based on the fact that high-concentration organic waste water enters the reaction layer, and the sewage cannot fully contact and react with the granular sludge in the reaction layer, resulting in slow reaction, low removal efficiency, uneven water temperature, and floating hollow granular sludge above the three-phase separator, etc. To solve the problem, an anaerobic external circulation system was constructed to achieve the purpose of strengthening the removal of pollutants, controlling the constant water temperature, and promoting the replacement and growth of new and old granular sludge, which significantly improved the removal efficiency and provided a guarantee for alleviating the workload of subsequent biochemical reactions.
发明内容Contents of the invention
本发明的目的是为了克服传统UASB厌氧反应器污水与微生物接触不充分,反应器内部水温不均匀,中空颗粒污泥上浮等问题,提供一种用于处理高浓度造纸废水的UASB反应器。The purpose of the present invention is to provide a UASB reactor for treating high-concentration papermaking wastewater in order to overcome the problems of insufficient contact between sewage and microorganisms in traditional UASB anaerobic reactors, uneven water temperature inside the reactor, and floating of hollow particle sludge.
本发明根据UASB厌氧反应器外部循环带动反应器内部水流流动,冲击反应层颗粒污泥,克服传统UASB污水和微生物接触不充分的缺点,对反应器内部水温进行均化,对中空污泥进行破坏,促进新老颗粒污泥更替生长,提高了厌氧反应效率。其具体方案是:一种用于处理高浓度造纸废水的UASB外循环系统,其特征在于:该系统包括罐体(1)、进水口(3)、布水器(4)、通孔(5)、循环管路出水口(7)、循环泵(6)、循环管路进水口(8)、出水口(9)、沼气收集管(14)、沼气收集器(12)、出气口(11)、溢流堰(13)、温度计探头(2)、三相分离器(15)、温度计探头(16)、流量计(17)、止回阀(18),进水口和出水口分别设置在反应器的下端和上端,循环管路系统各部由管道进行连接。According to the external circulation of the UASB anaerobic reactor, the water flow inside the reactor is driven to impact the granular sludge in the reaction layer, so as to overcome the shortcomings of insufficient contact between the traditional UASB sewage and microorganisms, homogenize the water temperature inside the reactor, and carry out the hollow sludge treatment. Destruction, promote the replacement growth of new and old granular sludge, and improve the efficiency of anaerobic reaction. The specific solution is: a UASB external circulation system for treating high-concentration papermaking wastewater, which is characterized in that: the system includes a tank body (1), a water inlet (3), a water distributor (4), a through hole (5 ), circulation pipeline water outlet (7), circulation pump (6), circulation pipeline water inlet (8), water outlet (9), biogas collection pipe (14), biogas collector (12), gas outlet (11 ), overflow weir (13), thermometer probe (2), three-phase separator (15), thermometer probe (16), flow meter (17), check valve (18), water inlet and outlet are respectively set in The lower end and upper end of the reactor, and each part of the circulation piping system are connected by pipes.
优选的,所述的一种用于处理高浓度造纸废水的UASB反应器,其特征在于:所述布水器(4)铺设在反应器底部,所述通孔(5)密布在布水器(4)上。Preferably, the UASB reactor for treating high-concentration papermaking wastewater is characterized in that: the water distributor (4) is laid on the bottom of the reactor, and the through holes (5) are densely covered in the water distributor (4) up.
优选的,所述的一种用于处理高浓度造纸废水的UASB反应器,其特征在于:进水口(3)与布水器(4)连接,位于反应器主体(1)底部。Preferably, the UASB reactor for treating high-concentration papermaking wastewater is characterized in that: the water inlet (3) is connected to the water distributor (4) and is located at the bottom of the reactor main body (1).
优选的,所述的一种用于处理高浓度造纸废水的UASB反应器,其特征在于:循环管路进水口(8)位于三相分离器(15)上方。Preferably, the UASB reactor for treating high-concentration papermaking wastewater is characterized in that: the water inlet (8) of the circulation pipeline is located above the three-phase separator (15).
优选的,所述的一种用于处理高浓度造纸废水的UASB反应器,其特征在于:循环管路出水口(7)位于布水器(4)上方。Preferably, the UASB reactor for treating high-concentration papermaking wastewater is characterized in that: the water outlet (7) of the circulation pipeline is located above the water distributor (4).
优选的,所述的一种用于处理高浓度造纸废水的UASB反应器,其特征在于:所述三相分离器(15)截面的性状为三角形,顶角角度在50°~60°之间,其顶角处开有沼气收集管(14),所述沼气收集管(14)与沼气收集器(12)连接,所述所述止回阀(18)位于沼气收集管(14)中段。Preferably, the UASB reactor for treating high-concentration papermaking wastewater is characterized in that: the shape of the section of the three-phase separator (15) is triangular, and the vertex angle is between 50° and 60° There is a biogas collection pipe (14) at the top corner, the biogas collection pipe (14) is connected to the biogas collector (12), and the check valve (18) is located in the middle section of the biogas collection pipe (14).
优选的,所述的一种用于处理高浓度造纸废水的UASB反应器,其特征在于:所述弯头(10)位于沼气收集器(12)内,并与沼气收集管(14)链接。Preferably, the UASB reactor for treating high-concentration papermaking wastewater is characterized in that: the elbow (10) is located in the biogas collector (12) and connected with the biogas collection pipe (14).
优选的,所述的一种用于处理高浓度造纸废水的UASB反应器,其特征在于:所述循环泵(6)为螺旋泵,其与循环管路出水口(7)、流量计(18)和循环管路进水口(8)连接。Preferably, the UASB reactor for treating high-concentration papermaking wastewater is characterized in that: the circulation pump (6) is a screw pump, which is connected with the circulation pipeline outlet (7), flow meter (18 ) to the water inlet (8) of the circulation line.
优选的,所述的一种用于处理高浓度造纸废水的UASB反应器,其特征在于:所述温度计探头-1(2)、温度计探头-2(16)分别位于反应器1/3、2/3处。Preferably, the UASB reactor for treating high-concentration papermaking wastewater is characterized in that: the thermometer probe-1 (2) and the thermometer probe-2 (16) are respectively located in the
附图说明Description of drawings
图1是本发明的总体结构示意图,图中标号:1:UASB反应器主体;2:温度计探头-1;3:进水口;4:布水器;5:通孔;6:循环泵;7:循环管路出水口;8:循环管路进水口;9:出水口;10:弯头;11:出气口;12:沼气收集器;13:溢流堰;14:沼气收集管;15:三相分离器;16:温度计探头-2;17:流量计;18:止回阀。Fig. 1 is a schematic diagram of the overall structure of the present invention, the number in the figure: 1: UASB reactor main body; 2: thermometer probe-1; 3: water inlet; 4: water distributor; 5: through hole; 6: circulating pump; 7 : circulation pipeline water outlet; 8: circulation pipeline water inlet; 9: water outlet; 10: elbow; 11: gas outlet; 12: biogas collector; 13: overflow weir; 14: biogas collection pipe; 15: Three-phase separator; 16: thermometer probe-2; 17: flow meter; 18: check valve.
图2是循环泵开启前后COD去除效率。Figure 2 is the COD removal efficiency before and after the circulation pump is turned on.
图3循环泵开启前后温度变化。Figure 3 Temperature change before and after the circulation pump is turned on.
具体实施方式detailed description
为实现本发明实施例的目的、技术方案和优点,下面将结合以下实施例,对本发明进一步说明。显然,所描述的实施例是本发明的一部分实施例,而不是全部的实施例。基于所描述的本发明的实施例,本领域普通技术人员在无需创造性劳动的前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to achieve the objectives, technical solutions and advantages of the embodiments of the present invention, the present invention will be further described below in conjunction with the following embodiments. Apparently, the described embodiments are some, not all, embodiments of the present invention. Based on the described embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
本发明提出的是一种用于处理高浓度造纸废水的UASB反应器,包括如下步骤:What the present invention proposes is a kind of UASB reactor for the treatment of high-concentration papermaking wastewater, comprising the following steps:
(1)构建储水系统,并与UASB进水口连接;(1) Build a water storage system and connect it to the UASB water inlet;
(2)构建UASB系统,采用有机玻璃材质制作配件并组装;(2) Construct the UASB system, use plexiglass to make accessories and assemble them;
(2)准备足量的厌氧颗粒污泥;(2) Prepare a sufficient amount of anaerobic granular sludge;
(3)填充厌氧颗粒污泥;(3) Filling with anaerobic granular sludge;
(4)从造纸厂取废水,进行微生物驯化,开始进水,驯化一周;(4) Take wastewater from the paper mill, carry out microbial domestication, start water intake, and domesticate for a week;
(6)正式运行。(6) Formal operation.
以下结合具体实例,对本发明进行详细说明。The present invention will be described in detail below in conjunction with specific examples.
实施例一:造纸产业园污水厂原水,COD 4500 mg/L、水温20℃;UASB水力停留时间:13.5 h。Example 1: Raw water from sewage plant in paper industry park, COD 4500 mg/L,
每天固定两个时间段,采集系统内的进水水样、出水水样,使用标准方法进行测定COD的浓度(TU-1810, PUXI, China),使用数显温度计(TDM-280)进行水温测定。所用的所有试剂均为分析级试剂,分析一式两份,经过20天水温和COD数据监测,发现在开启循环泵以后,COD去除效率较开启循环泵前提高10%左右;反应器内部水温更加稳定,变化幅度较小。Set two time periods every day to collect the influent and effluent water samples in the system, use the standard method to measure the COD concentration (TU-1810, PUXI, China), and use the digital display thermometer (TDM-280) to measure the water temperature . All reagents used are analytical grade reagents, analyzed in duplicate, after 20 days of water temperature and COD data monitoring, it is found that after the circulation pump is turned on, the COD removal efficiency is about 10% higher than before the circulation pump is turned on; the water temperature inside the reactor is more stable, The change is small.
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Cited By (1)
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Application publication date: 20230106 |
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