CN202186908U - 聚截除油器 - Google Patents
聚截除油器 Download PDFInfo
- Publication number
- CN202186908U CN202186908U CN2011203216599U CN201120321659U CN202186908U CN 202186908 U CN202186908 U CN 202186908U CN 2011203216599 U CN2011203216599 U CN 2011203216599U CN 201120321659 U CN201120321659 U CN 201120321659U CN 202186908 U CN202186908 U CN 202186908U
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- oil
- amputation
- oil tank
- coalescence
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- 238000004581 coalescence Methods 0.000 title claims abstract description 25
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound 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O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances data:image/svg+xml;base64,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 data:image/svg+xml;base64,PD94bWwgdmVyc2lvbj0nMS4wJyBlbmNvZGluZz0naXNvLTg4NTktMSc/Pgo8c3ZnIHZlcnNpb249JzEuMScgYmFzZVByb2ZpbGU9J2Z1bGwnCiAgICAgICAgICAgICAgeG1sbnM9J2h0dHA6Ly93d3cudzMub3JnLzIwMDAvc3ZnJwogICAgICAgICAgICAgICAgICAgICAgeG1sbnM6cmRraXQ9J2h0dHA6Ly93d3cucmRraXQub3JnL3htbCcKICAgICAgICAgICAgICAgICAgICAgIHhtbG5zOnhsaW5rPSdodHRwOi8vd3d3LnczLm9yZy8xOTk5L3hsaW5rJwogICAgICAgICAgICAgICAgICB4bWw6c3BhY2U9J3ByZXNlcnZlJwp3aWR0aD0nODVweCcgaGVpZ2h0PSc4NXB4JyB2aWV3Qm94PScwIDAgODUgODUnPgo8IS0tIEVORCBPRiBIRUFERVIgLS0+CjxyZWN0IHN0eWxlPSdvcGFjaXR5OjEuMDtmaWxsOiNGRkZGRkY7c3Ryb2tlOm5vbmUnIHdpZHRoPSc4NS4wJyBoZWlnaHQ9Jzg1LjAnIHg9JzAuMCcgeT0nMC4wJz4gPC9yZWN0Pgo8dGV4dCB4PScxMy4zJyB5PSc1My42JyBjbGFzcz0nYXRvbS0wJyBzdHlsZT0nZm9udC1zaXplOjIzcHg7Zm9udC1zdHlsZTpub3JtYWw7Zm9udC13ZWlnaHQ6bm9ybWFsO2ZpbGwtb3BhY2l0eToxO3N0cm9rZTpub25lO2ZvbnQtZmFtaWx5OnNhbnMtc2VyaWY7dGV4dC1hbmNob3I6c3RhcnQ7ZmlsbDojRTg0MjM1JyA+SDwvdGV4dD4KPHRleHQgeD0nMjguMicgeT0nNjIuOScgY2xhc3M9J2F0b20tMCcgc3R5bGU9J2ZvbnQtc2l6ZToxNXB4O2ZvbnQtc3R5bGU6bm9ybWFsO2ZvbnQtd2VpZ2h0Om5vcm1hbDtmaWxsLW9wYWNpdHk6MTtzdHJva2U6bm9uZTtmb250LWZhbWlseTpzYW5zLXNlcmlmO3RleHQtYW5jaG9yOnN0YXJ0O2ZpbGw6I0U4NDIzNScgPjI8L3RleHQ+Cjx0ZXh0IHg9JzM1LjAnIHk9JzUzLjYnIGNsYXNzPSdhdG9tLTAnIHN0eWxlPSdmb250LXNpemU6MjNweDtmb250LXN0eWxlOm5vcm1hbDtmb250LXdlaWdodDpub3JtYWw7ZmlsbC1vcGFjaXR5OjE7c3Ryb2tlOm5vbmU7Zm9udC1mYW1pbHk6c2Fucy1zZXJpZjt0ZXh0LWFuY2hvcjpzdGFydDtmaWxsOiNFODQyMzUnID5PPC90ZXh0Pgo8L3N2Zz4K O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 11
- 238000009826 distribution Methods 0.000 claims abstract description 10
- 238000005273 aeration Methods 0.000 claims abstract description 5
- 230000000875 corresponding Effects 0.000 claims abstract description 5
- 238000000926 separation method Methods 0.000 claims abstract description 4
- 238000002266 amputation Methods 0.000 claims description 56
- SZVJSHCCFOBDDC-UHFFFAOYSA-N Iron(II,III) oxide Chemical compound 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O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 22
- 239000004576 sand Substances 0.000 claims description 14
- 239000000377 silicon dioxide Substances 0.000 claims description 14
- 238000000605 extraction Methods 0.000 claims description 8
- 230000000630 rising Effects 0.000 claims description 7
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000005755 formation reaction Methods 0.000 claims description 2
- 239000010865 sewage Substances 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 9
- 239000006004 Quartz sand Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 238000011084 recovery Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 6
- 239000007787 solid Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 238000004140 cleaning Methods 0.000 description 2
- 238000003795 desorption Methods 0.000 description 2
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- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
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- 239000002351 wastewater Substances 0.000 description 1
Abstract
一种聚截除油器。主要用来解决现有技术中存在的沉降分离效果差，组合除油器和横向流除油器处理后的系统出水不达标的问题。其特征在于：所述聚截除油器由串联连接的八级聚截除油罐构成，进水管连接至一级砾石聚截除油罐的入口，出水管由二级石英砂聚截除油罐的出口引出；其中，聚截除油罐之间通过带有液流出口的隔板分隔，聚截除油罐内填充有对应的聚结材料，聚截除油罐的底部分布有带曝气口的布气管，每级聚截除油罐的上部开有对应的油污出口阀；聚截除油器还包括一根位于除油器上部的排油汇管和一根位于除油器下部的进气管，油污出口阀和布气管分别对应连通于排油汇管和进气管上。本种除油器可以充分保证除油器对三次采油污水的除油效果。
Description
聚截除油器
技术领域
[0001] 本实用新型涉及一种含油污水处理装置，尤其是涉及一种应用于油田聚驱采油污水处理领域中的含油污水处理装置。
背景技术
[0002] 目前，油田上已经广泛应用了利用聚合物的三次采油方法，但是由此引发的一个新问题就是：污水中聚合物含量高，污水中的聚合物集中在油水界面上，与表面活性剂一起形成强度较大、弹性良好的复合膜，导致水体粘度大、破乳困难，使得现有的沉降除油装置处理效率下降，严重影响了对含油污水的处理效果。此外，现有的横向流除油器以及组合除油器，由于其没有反冲洗系统不能进行反冲洗系统，因此对于造成堵塞的内部结构无法进行彻底清洗疏通，也由此导致了这种现有的污水处理装置对于三采污水处理效率较低，处理完毕的系统出水难以达标。
发明内容
[0003] 为了解决背景技术提出的现有技术中存在的问题，本实用新型提供了一种聚截除油器，本种聚截除油器在结构上分为八级除油构造，能够解决现有技术中存在的沉降分离效果差，组合除油器和横向流除油器处理后的系统出水不达标的问题，可以充分保证除油器的除油效果。
[0004] 本实用新型的技术方案是：该种聚截除油器，包括进水管和出水管，其中，所述聚截除油器由串联连接的一级砾石聚截除油罐、二级砾石聚截除油罐、一级陶粒聚截除油罐、 二级陶粒聚截除油罐、一级磁铁矿聚截除油罐、二级磁铁矿聚截除油罐、一级石英砂聚截除油罐和二级石英砂聚截除油罐构成，进水管连接至一级砾石聚截除油罐的入口，出水管由二级石英砂聚截除油罐的出口引出；其中，上述每级聚截除油罐之间通过带有液流出口的隔板分隔，每级聚截除油罐内填充有对应的聚结材料，所述每级聚截除油罐的底部分布有带曝气口的布气管，所述每级聚截除油罐的上部开有对应的油污出口阀；所述聚截除油器还包括一根位于除油器上部的排油汇管和一根位于除油器下部的进气管，所述若干油污出口阀和布气管分别对应连通于排油汇管和进气管上。
[0005] 本实用新型具有如下有益效果：本种除油器在结构上分为八级除油构造，含油污水从一级进口以水平流方式流经除油器的每一级，每一级均填充聚结材料，其中第一、二级填充砾石，三、四级填充陶粒，五、六级填充石英砂，七、八级填充磁铁矿。填充的聚结材料具有更小孔隙率和更大比表面积的特点。污水在流经聚结材料过程中会形成一个类过滤过程，利用物理聚结作用来强化破乳效果，增加颗粒之间的碰撞机会，最终实现聚结功能。同时，由于聚结材料孔隙率小，对污水中的油和悬浮物具有较强的截留作用，通过聚结和截留作用实现油和悬浮固体的去除。另外，在本种除油器中，在每一级设置曝气系统，对进入每一级内的污水进行气浮作用。利用曝气形成的微小气泡将截留油和悬浮固体带至罐体上方，由排油管线排走，这样就可以在进行气浮的同时利用气泡的携带作用将截留油排出，达到了对聚结材料进行清洗再生的目的，避免聚结材料堵塞导致处理效率降低的问题。
[0006] 附图说明：
[0007] 图1是本实用新型的整体结构示意图。
[0008] 图中1-进水管，2-出水管，3-进气管，4-布气管，5- 一级砾石聚截除油罐，6_ 二级砾石聚截除油罐，7-—级陶粒聚截除油罐，8-二级陶粒聚截除油罐，9-一级磁铁矿聚截除油罐，10- 二级磁铁矿聚截除油罐，11- 一级石英砂聚截除油罐，12- 二级石英砂聚截除油罐。
[0009] 具体实施方式：
[0010] 下面结合附图对本实用新型作进一步说明：
[0011] 如图1所示，该种聚截除油器，包括进水管1和出水管2，其中，所述聚截除油器由串联连接的一级砾石聚截除油罐5、二级砾石聚截除油罐6、一级陶粒聚截除油罐7、二级陶粒聚截除油罐8、一级磁铁矿聚截除油罐9、二级磁铁矿聚截除油罐10、一级石英砂聚截除油罐11和二级石英砂聚截除油罐12构成，进水管1连接至一级砾石聚截除油罐5的入口，出水管2由二级石英砂聚截除油罐12的出口引出；其中，上述每级聚截除油罐之间通过带有液流出口的隔板分隔，每级聚截除油罐内填充有对应的聚结材料，所述每级聚截除油罐的底部分布有带曝气口的布气管4，所述每级聚截除油罐的上部开有对应的油污出口阀 13 ；所述聚截除油器还包括一根位于除油器上部的排油汇管14和一根位于除油器下部的进气管3，所述若干油污出口阀13和布气管4分别对应连通于排油汇管14和进气管3上。
[0012] 本种除油器具体实施时，如图1所示，污水由进水管1进入除油器，污水依次流经一级砾石聚结除油罐5、二级砾石聚结除油罐6、一级陶粒聚截除油罐7、二级陶粒聚截除油罐8、一级磁铁矿聚截除油罐9、二级磁铁矿聚截除油罐10、一级石英砂聚截除油罐11和二级石英砂聚截除油罐12，每一级污水沿水平方向流动过程中，水中的油和悬浮固体依次被各级除油罐中的聚结材料截留，最终形成过滤完毕的系统出水经由出水管2排出。同时由空压机产生气体经由进气管3再由布气管4依次均勻分配给各级，由于气体产生浮力作用， 导致各级填料产生向上运动，截留油和杂质在浮力作用下亦向上运动，经由上方排油阀门 13收集后进入排油汇管14，排入收油罐。
[0013] 在利用本种除油器工作时，由于在处理过程中填料处于截留和脱附同时存在的状态，即截留污物的同时还利用气体的作用实现了脱附的过程，从而该设备无需进行反冲洗， 不易发生堵塞，能够保证系统出水中的油和悬浮固体的含量达到滤后水的指标要求。
4
Claims (1)
1. 一种聚截除油器，包括进水管（1)和出水管（2)，其特征在于：所述聚截除油器由串联连接的一级砾石聚截除油罐（5)、二级砾石聚截除油罐（6)、一级陶粒聚截除油罐（7)、二级陶粒聚截除油罐（8)、一级磁铁矿聚截除油罐（9)、二级磁铁矿聚截除油罐（10)、一级石英砂聚截除油罐（11)和二级石英砂聚截除油罐（12)构成，进水管（1)连接至一级砾石聚截除油罐（5)的入口，出水管（2)由二级石英砂聚截除油罐（12)的出口引出；其中，上述每级聚截除油罐之间通过带有液流出口的隔板分隔，每级聚截除油罐内填充有对应的聚结材料，所述每级聚截除油罐的底部分布有带曝气口的布气管（4)，所述每级聚截除油罐的上部开有对应的油污出口阀（13)；所述聚截除油器还包括一根位于除油器上部的排油汇管（14) 和一根位于除油器下部的进气管（3)，所述若干油污出口阀（13)和布气管（4)分别对应连通于排油汇管（14)和进气管（3)上。
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102826706A (zh) * | 2012-09-28 | 2012-12-19 | 湖南科技大学 | 一种油田采出水处理方法及设备 |
| CN105948286A (zh) * | 2016-05-16 | 2016-09-21 | 南京碧盾环保科技有限公司 | 一种针对闭式循环水系统含油污水旁滤除油净化组合装置 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102826706A (zh) * | 2012-09-28 | 2012-12-19 | 湖南科技大学 | 一种油田采出水处理方法及设备 |
| CN102826706B (zh) * | 2012-09-28 | 2014-02-12 | 湖南科技大学 | 一种油田采出水处理方法及设备 |
| CN105948286A (zh) * | 2016-05-16 | 2016-09-21 | 南京碧盾环保科技有限公司 | 一种针对闭式循环水系统含油污水旁滤除油净化组合装置 |
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