CN109020157A - 一种高含油废水污泥的处理方法 - Google Patents
一种高含油废水污泥的处理方法 Download PDFInfo
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- CN109020157A CN109020157A CN201811094185.1A CN201811094185A CN109020157A CN 109020157 A CN109020157 A CN 109020157A CN 201811094185 A CN201811094185 A CN 201811094185A CN 109020157 A CN109020157 A CN 109020157A
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- sludge
- delivered
- flocculation
- oil
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- 239000010802 sludge Substances 0.000 title claims abstract description 91
- 239000002351 wastewater Substances 0.000 title claims abstract description 15
- 238000003672 processing method Methods 0.000 title claims description 7
- 229920002401 polyacrylamide Polymers 0.000 claims abstract description 20
- 238000005189 flocculation Methods 0.000 claims abstract description 12
- 230000016615 flocculation Effects 0.000 claims abstract description 12
- 238000002156 mixing Methods 0.000 claims abstract description 10
- 150000001768 cations Chemical class 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nMzAwcHgnIGhlaWdodD0nMzAwcHgnIHZpZXdCb3g9JzAgMCAzMDAgMzAwJz4KPCEtLSBFTkQgT0YgSEVBREVSIC0tPgo8cmVjdCBzdHlsZT0nb3BhY2l0eToxLjA7ZmlsbDojRkZGRkZGO3N0cm9rZTpub25lJyB3aWR0aD0nMzAwLjAnIGhlaWdodD0nMzAwLjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8dGV4dCB4PScxMDAuNScgeT0nMTcwLjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5IPC90ZXh0Pgo8dGV4dCB4PScxMjYuMScgeT0nMTg2LjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6MjZweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID4yPC90ZXh0Pgo8dGV4dCB4PScxMzguMCcgeT0nMTcwLjAnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6NDBweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5PPC90ZXh0Pgo8L3N2Zz4K data:image/svg+xml;base64,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 O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000000463 material Substances 0.000 claims abstract description 8
- 238000003825 pressing Methods 0.000 claims abstract description 8
- 238000004939 coking Methods 0.000 claims abstract description 7
- 238000000926 separation method Methods 0.000 claims abstract description 5
- 238000003756 stirring Methods 0.000 claims abstract description 5
- -1 amine cation Chemical class 0.000 claims abstract description 4
- 238000001035 drying Methods 0.000 claims abstract description 4
- NRADCUWKNUKPHY-UHFFFAOYSA-N oxalonitrile;phenol Chemical compound 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- 230000000694 effects Effects 0.000 abstract description 4
- 239000007787 solid Substances 0.000 abstract description 3
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- 238000000034 method Methods 0.000 description 5
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- 238000004065 wastewater treatment Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drugs Drugs 0.000 description 1
- 230000003311 flocculating Effects 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
Abstract
本发明涉及一种高含油废水污泥的处理方法,包括有:制絮凝剂:将水和聚丙烯酰胺阳离子按比例注入到PAM溶解池中,启动溶液搅拌器搅拌,搅拌均匀后,制成溶液;污泥配制:焦化废水高含油有机污泥与无机污泥输送至污泥混合池;物料输送:将配泥池配制好的污泥输送至污泥反应槽中,同时PAM阳离子溶解池中的絮凝剂溶液输送至污泥反应槽中;搅拌絮凝:启动污泥反应槽的搅拌器,当发现污泥反应槽中有絮凝物出现时,启动污泥泵,将絮凝物料输送至压滤机中;干化处理:经过絮凝反应沉淀的污泥送入压滤机进行泥水分离,压滤后污泥外运至酚氰料场配矿处理。具有污泥固液分离效果好,压滤性能好、药剂消耗少等特点。
Description
一种高含油废水污泥的处理方法
技术领域
[0001] 本发明属于废水处理工艺技术领域,涉及一种对焦化废水进行处理的高含油废水 污泥的处理方法。
背景技术
[0002] 污泥处理是焦化废水活性污泥生化处理法的重要组成部分,在污泥处理过程中, 需要对污泥进行浓缩,然后再进行固、液分离,压滤后的千污泥外运处理。原污泥处理系统 配制两套(图1),分别对应处理有机污泥和无机污泥。压搾有机污泥时,通过栗送至反应槽 1,在此加入PAM进行絮凝,然后再送至带式压滤机1压榨;压榨无机污泥时,通过栗送至反应 槽2,在此加入PAM进行絮凝,然后再送至带式压滤机2压榨。有机污泥和无机污泥分开压搾, 独立运行。生产运行中处理含油量高的有机污泥时,存在耗药(PAM阳离子)大、絮凝效果差、 泥量小、带式压滤机2滤带易粘附污泥,冲洗水量大、滤带容易损坏,检修频繁,生产效率低, 运行成本高等问题。
发明内容
[0003] 为了克服现有技术的上述缺点,本发明提供一种高含油废水污泥的处理方法,它 将原设计中的有机污泥池2改成污泥混合池,并将有机污泥和无机污泥在污泥混合池按一 定比例混合配制,具有污泥固液分离效果好,压滤性能好、药剂消耗少等特点。
[0004] 本发明解决其技术问题所采用的技术方案是:一种高含油废水污泥的处理方法, 包括有: 1、 制絮凝剂:将水和聚丙烯酰胺阳离子按1000:2-3的比例注入到PAM溶解池中,启动溶 液搅拌器在转速为63-85转/分下进行搅拌,搅拌均匀后,制成质量百分比浓度为〇. 2-0.3% 的溶液; 2、 污泥配制:焦化废水高含油有机污泥与无机污泥按3:1输送至污泥混合池,在此通过 曝气混匀; 3、 物料输送:将配泥池配制好的污泥通过污泥输送泵按流量为10-15mVh输送至污泥 反应槽中,同时PAM (阳离子)溶解池中的絮凝剂溶液通过PAM (阳离子)输送栗,按流量为 100-250L/h的速度输送至污泥反应槽中; 4、 撹拌絮凝:启动污泥反应槽的搅拌器,控制搅拌器的转速为60-90转/分进行搅拌,当 发现污泥反应槽中有大量絮凝物出现时,启动污泥栗,将絮凝物料输送至压滤机中; 5、 干化处理:经过絮凝反应沉淀的污泥送入压滤机进行泥水分离,压滤后污泥外运至 酚氰料场配矿处理。
[0005]本发明的积极效果是:利用焦化废水处理中产生的高油有机污泥、无机污泥的性 能配制污泥,提高污泥压滤性能,工艺简单,操作方便,不需要复杂的污泥与PAM溶液的比例 调试;本发明所需装置少,操作简单,污泥压滤效率高,对比以前有机污泥压泥,泥量由 1 • 7t/h提升至2• 8t/h;PAM阳离子耗量由1 • 2kg每吨污泥降至约〇• 8kg每吨污泥;本发明压 滤效果好,污泥含水率比以前压滤后的有机污泥含水率能减低约20%,污泥含水率稳定在 70%左右;能够连续稳定压泥,污泥处理量大,提高了劳动效率,有效避免了因污泥不及时影 响废水处理系统的正常运行。
附图说明
[0006] 图1是现有高含油废水污泥处理工艺示意图。
具体实施方式
[0007] 下面结合实施例对本发明进一步说明。
[0008] 一种高含油废水污泥的处理方法,包括有: 1、 制絮凝剂:将水和聚丙烯酰胺阳离子按1000:2-3的比例注入到PAM溶解池中,启动溶 液搅拌器在转速为63-85转/分下进行搅拌,搅拌均匀后,制成质量百分比浓度为0.2-0.3% 的溶液; 2、 污泥配制:焦化废水高含油有机污泥与无机污泥按3:1输送至污泥混合池,在此通过 曝气混匀; 3、 物料输送:将配泥池配制好的污泥通过污泥输送泵按流量为1〇-I5m3/h输送至污泥 反应槽中,同时PAM (阳离子)溶解池中的絮凝剂溶液通过PAM (阳离子)输送栗,按流量为 100-250L/h的速度输送至污泥反应槽中; 4、 搅拌絮凝:启动污泥反应槽的搅拌器,控制搅拌器的转速为60-90转/分进行搅拌,当 发现污泥反应槽中有大量絮凝物出现时,启动污泥栗,将絮凝物料输送至压滤机中; 5、 干化处理:经过絮凝反应沉淀的污泥送入压滤机进行泥水分离,压滤后污泥外运至 酚氰料场配矿处理。 ^
[0009]以上仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的原则之内,所 作任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。 ' ’
Claims (1)
1.一种高含油废水污泥的处理方法,其特征在于包括有: (1) 制絮凝剂:将水和聚丙烯酰胺阳离子按1000: 2-3的比例注入到PAM溶解池中,启动 溶液搅拌器在转速为63-85转/分下进行搅拌,搅拌均匀后,制成质量百分比浓度为〇.2一 0.3%的溶液; (2) 、污泥配制:焦化废水高含油有机污泥与无机污泥按3:1输送至污泥混合池,在此通 过曝气混匀; (3) 物料输送:将配泥池配制好的污泥通过污泥输送泵按流量为10—15m3/h输送至污泥 反应槽中,同时PAM阳离子溶解池中的絮凝剂溶液通过PAM阳离子输送泵,按流量为100-250L/h的速度输送至污泥反应槽中; (4) 搅拌絮凝:启动污泥反应槽的搅拌器,控制搅拌器的转速为60-90转/分进行搅拌, 当发现污泥反应槽中有大量絮凝物出现时,启动污泥泵,将絮凝物料输送至压滤机中; (5) 干化处理:经过絮凝反应沉淀的污泥送入压滤机进行泥水分离,压滤后污泥外运至 酚氰料场配矿处理。
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