CN205151962U - 一种制药发酵污水处理罐 - Google Patents
一种制药发酵污水处理罐 Download PDFInfo
- Publication number
- CN205151962U CN205151962U CN201520966989.1U CN201520966989U CN205151962U CN 205151962 U CN205151962 U CN 205151962U CN 201520966989 U CN201520966989 U CN 201520966989U CN 205151962 U CN205151962 U CN 205151962U
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- catalytic oxidation
- oxidation room
- tank body
- water
- room
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- 239000010865 sewage Substances 0.000 title claims abstract description 19
- 238000000855 fermentation Methods 0.000 title claims abstract description 8
- 230000004151 fermentation Effects 0.000 title claims abstract description 8
- 230000003197 catalytic Effects 0.000 claims abstract description 40
- 230000003647 oxidation Effects 0.000 claims abstract description 40
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 40
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 239000004575 stone Substances 0.000 claims abstract description 11
- 239000000126 substance Substances 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 5
- 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 description 27
- 238000005202 decontamination Methods 0.000 claims description 19
- 230000003588 decontaminative Effects 0.000 claims description 19
- 238000001914 filtration Methods 0.000 claims description 10
- 230000004048 modification Effects 0.000 claims description 9
- 238000006011 modification reaction Methods 0.000 claims description 9
- 239000000945 filler Substances 0.000 claims description 8
- 230000000630 rising Effects 0.000 claims description 8
- 238000005273 aeration Methods 0.000 claims description 5
- 239000003153 chemical reaction reagent Substances 0.000 abstract description 3
- 239000003599 detergent Substances 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 4
- CVTZKFWZDBJAHE-UHFFFAOYSA-N [N].N Chemical compound 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- 125000001997 phenyl group Chemical group 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[H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 150000003016 phosphoric acids Chemical class 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound 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Abstract
本实用新型公开一种制药发酵污水处理罐，包括罐体，所述罐体内设有第一接触氧化室、第二接触氧化室、净化室和混合反应室，所述第一接触氧化室和第二接触氧化室内设有过滤网筒，所述过滤网筒顶部中心连接有转轴，转轴的另一端伸出罐体连接一电机，所述净化室内的相对两侧上分别设有数块挡水板，所述净化室内还设有改性浮石填料，所述改性浮石填料填充在挡水板之间，所述混合反应室内上部为反应仓，下部为沉降仓，所述反应仓内设有加热管和加药管，沉降仓的一侧上部设有出水管，出水管与罐体的出水口连通。本实用新型采用物理过滤和化学过滤的方式，使得污水处理彻底，减小了化学试剂的使用，降低了去污的成本。
Description
技术领域
[0001]本实用新型属于制药污水处理技术领域，具体涉及一种制药发酵污水处理罐。
背景技术
[0002]生物制药废水有机物浓度高，成分复杂，含有胺类、酸类、破乳剂等污染物质。此夕卜，水中还含有难以降解的苯环类物质和较高的磷酸盐，废水C0D、磷含量高，如果不能达标排放，造成水域环境的恶化给流域内的工农业生产和居民生活带来了严重的后果，妨碍地区经济持续、稳定地发展，所以必须经处理后，才能达标排放，所以就需要一种处理成本低且高效环保的生物制药污水净化系统。
实用新型内容
[0003]本实用新型所要解决的技术问题便是针对上述现有技术的不足，提供一种制药发酵污水处理罐，它结构简单、设计合理，污水处理效果好，且处理成本低廉，大大降低了制药的生产成本。
[0004]本实用新型所采用的技术方案是:一种制药发酵污水处理罐，包括罐体，所述罐体的一端接有进水口，另一端接有出水口，所述罐体内设有第一接触氧化室、第二接触氧化室、净化室和混合反应室，所述第一接触氧化室的一端设有进水管，所述进水管与罐体的进水口连通，所述第一接触氧化室与第二接触氧化室之间通过管道连接，所述第一接触氧化室和第二接触氧化室内设有过滤网筒，所述过滤网筒顶部中心连接有转轴，转轴的另一端伸出罐体连接一电机，所述第二接触氧化室与净化室之间通过管道连通，净化室与混合反应室之间通过管道连接，所述净化室内的相对两侧上分别设有数块挡水板，相对两侧上设置的挡水板交错分布，所述净化室内还设有改性浮石填料，所述改性浮石填料填充在挡水板之间，所述混合反应室内上部为反应仓，下部为沉降仓，所述反应仓内设有加热管和加药管，沉降仓的一侧上部设有出水管，出水管与罐体的出水口连通。
[0005]作为优选，所述第一接触氧化室与第二接触氧化室底部设有曝气管。
[0006]本实用新型的有益效果在于:本实用新型结构简单、设计合理，采用物理过滤和化学过滤的方式，使得污水处理彻底，减小了化学试剂的使用，降低了去污的成本，同时采用改性浮石净化污水，大大降低了污水中的氨氮污染物，使得污水中氨氮污染物达到排放标准。
附图说明
[0007 ]图I为本实用新型结构不意图。
[0008]图中：I、罐体;2、进水口； 3、出水口； 4、第一接触氧化室;5、第二接触氧化室;6、净化室;7、混合反应室;8、进水管;9、过滤网筒；10、转轴；11、电机;12、挡水板;13、改性浮石填料;14、加热管；15、加药管；16、出水管；17、曝气管;71、反应仓;72、沉降仓。
具体实施方式
[0009]下面将结合附图及具体实施例对本实用新型作进一步详细说明。
[0010]实施例I ：本实用新型包括罐体I，所述罐体I的一端接有进水口 2，另一端接有出水口 3，所述罐体I内设有第一接触氧化室4、第二接触氧化室5、净化室6和混合反应室7，所述第一接触氧化室4的一端设有进水管8，所述进水管8与罐体I的进水口 2连通，所述第一接触氧化室4与第二接触氧化室5之间通过管道连接，所述第一接触氧化室4和第二接触氧化室5内设有过滤网筒9，所述过滤网筒9顶部中心连接有转轴10，转轴10的另一端伸出罐体I连接一电机11，所述第二接触氧化室5与净化室6之间通过管道连通，净化室6与混合反应室7之间通过管道连接，所述净化室6内的相对两侧上分别设有数块挡水板12，相对两侧上设置的挡水板12交错分布，所述净化室6内还设有改性浮石填料13，所述改性浮石填料13填充在挡水板12之间，所述混合反应室7内上部为反应仓71，下部为沉降仓72，所述反应仓71内设有加热管14和加药管15，沉降仓72的一侧上部设有出水管16，出水管16与罐体I的出水口3连通。
[0011]实施例2:与上述实施例I相同，其中上述第一接触氧化室4与第二接触氧化室5底部设有曝气管17。
[0012]本实用新型将污水通过进水口2进入罐体I，从进水管8进入第一接触氧化室4后，依次经过第二接触氧化室5、净化室6和混合反应室7后，从出水管16排出，在第一接触氧化室4和第二接触氧化室5中，通过旋转的过滤网筒9，将污水中的固体杂质进行过滤，并通过曝气管17对污水进行氧化处理，在净化室6内通过改性浮石填料13净化污水中的氨氮污染物，在混合反应室7中通过加入酸性或碱性试剂来使污水PH达到中性，最后通过混合反应室7的沉降仓72沉降后排出。
Claims (2)
1. 一种制药发酵污水处理罐，包括罐体（I)，所述罐体（I)的一端接有进水口（2)，另一端接有出水口（3)，其特征在于:所述罐体（I)内设有第一接触氧化室(4)、第二接触氧化室(5)、净化室(6)和混合反应室(7)，所述第一接触氧化室(4)的一端设有进水管(8)，所述进水管(8)与罐体（I)的进水口（2)连通，所述第一接触氧化室(4)与第二接触氧化室(5)之间通过管道连接，所述第一接触氧化室(4)和第二接触氧化室(5)内设有过滤网筒(9)，所述过滤网筒(9)顶部中心连接有转轴（10)，转轴（10)的另一端伸出罐体（I)连接一电机（11)，所述第二接触氧化室(5)与净化室(6)之间通过管道连通，净化室(6)与混合反应室(7)之间通过管道连接，所述净化室(6)内的相对两侧上分别设有数块挡水板(12)，相对两侧上设置的挡水板(12)交错分布，所述净化室(6)内还设有改性浮石填料(13)，所述改性浮石填料(13)填充在挡水板（12)之间，所述混合反应室(7)内上部为反应仓(71)，下部为沉降仓(72)，所述反应仓(71)内设有加热管（14)和加药管（15)，沉降仓(72)的一侧上部设有出水管（16)，出水管（16)与罐体(I)的出水口（3)连通。
2.根据权利要求I所述的一种制药发酵污水处理罐，其特征在于:所述第一接触氧化室(4)与第二接触氧化室(5)底部设有曝气管（17)。
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108264167A (zh) * | 2018-03-22 | 2018-07-10 | 赵锦山 | 一种离心分离式污水处理装置 |
| CN108383329A (zh) * | 2018-03-22 | 2018-08-10 | 赵海平 | 一种直跌式污水溶气处理装置 |
| CN108585352A (zh) * | 2018-04-26 | 2018-09-28 | 杭州金知科技有限公司 | 一种急速增氧污水处理装置 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN108264167A (zh) * | 2018-03-22 | 2018-07-10 | 赵锦山 | 一种离心分离式污水处理装置 |
| CN108383329A (zh) * | 2018-03-22 | 2018-08-10 | 赵海平 | 一种直跌式污水溶气处理装置 |
| CN108585352A (zh) * | 2018-04-26 | 2018-09-28 | 杭州金知科技有限公司 | 一种急速增氧污水处理装置 |
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