CN213680155U - Immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment - Google Patents
Immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment Download PDFInfo
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- CN213680155U CN213680155U CN202022352237.XU CN202022352237U CN213680155U CN 213680155 U CN213680155 U CN 213680155U CN 202022352237 U CN202022352237 U CN 202022352237U CN 213680155 U CN213680155 U CN 213680155U
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Abstract
The utility model belongs to the technical field of waste water is used, specifically disclose an submergence formula ultrafiltration system for phenol cyanogen waste water treatment, produce pond, first self-cleaning filter, second self-cleaning filter, third self-cleaning filter, first membrane pond, second membrane pond, third membrane pond, first vacuum tank, second vacuum tank, third vacuum tank, first PMUF produce water pump, second PMUF produce water pump and third PMUF produce water pump etc. including OTA. The utility model discloses a be applied to phenol cyanogen waste water treatment's submergence formula ultrafiltration system's beneficial effect lies in: the device has reasonable design, can complete the efficient, safe and stable treatment of phenol-cyanogen wastewater, realizes the energy-saving, environment-friendly and safe wastewater treatment operation, and has strong practicability.
Description
Technical Field
The utility model belongs to the technical field of waste water is used, concretely relates to be applied to phenol cyanogen waste water treatment's submergence formula ultrafiltration system.
Background
The waste water containing phenol, cyanogen, sulfide and oil generated in the coal coking process.
The water vapor generated in the coke oven is cooled by a primary cooler together with the raw coke oven gas to form condensed water, which is called residual ammonia water, contains high-concentration ammonia, phenol, cyanogen, sulfide and oil and is the main wastewater in the coking industry. In addition, the direct cooling water of final cooling of coal gas, the direct steam condensation separation water of crude benzene processing, the direct steam condensation separation water of refined benzene processing, the direct steam condensation separation water of tar refining processing, washing water, workshop or equipment cleaning water and the like, and the residual ammonia water of the wastewater is called phenol-cyanogen wastewater together, and the wastewater is large in amount and complex in components.
In order to meet the requirement of environmental protection in industrial production, the generated phenol-cyanogen wastewater needs to be treated efficiently, safely and stably.
Based on the problem, the utility model provides an submergence formula ultrafiltration system for phenol cyanogen waste water treatment.
SUMMERY OF THE UTILITY MODEL
Utility model purpose: the utility model aims at prior art not enough, provide a be applied to phenol cyanogen waste water treatment's submergence formula ultrafiltration system, its reasonable in design can accomplish the high-efficient, safe and stable processing in the proper order to phenol cyanogen waste water, realizes energy-conserving, environmental protection and safe waste water treatment operation, and the practicality is strong.
The technical scheme is as follows: the utility model provides an immersion ultrafiltration system for phenol-cyanogen wastewater treatment, including OTA product pond, first self-cleaning filter, second self-cleaning filter, third self-cleaning filter, first membrane pond, second membrane pond, third membrane pond, first vacuum tank, second vacuum tank, third vacuum tank, first PMUF product water pump, second PMUF product water pump, third PMUF product water pump; the OTA water producing pool is provided with an inclined plate sedimentation water inlet pipe, an OTA water producing pool water pipe respectively connected with the OTA water producing pool, a first self-cleaning filter, a second self-cleaning filter and a third self-cleaning filter, a first PMUF raw water pump, a second PMUF raw water pump and a third PMUF raw water pump respectively arranged on the OTA water producing pool water pipe, a first membrane pool guide pipe, a second membrane pool guide pipe and a third membrane pool guide pipe which are respectively connected with the first self-cleaning filter, the second self-cleaning filter, the third self-cleaning filter, the first membrane pool, the second membrane pool and the third membrane pool at two ends, a blast pipe respectively connected with the first membrane pool, the second membrane pool and the third membrane pool, and a first vacuum tank guide pipe, a second vacuum tank guide pipe and a third vacuum tank guide pipe which are respectively connected with the first membrane pool, the second membrane pool, the third membrane pool, the first vacuum tank, the second vacuum tank and the third vacuum tank, and a first tap water replenishing pipe, a second tap water replenishing pipe and a third tap water replenishing pipe which are respectively connected with the first vacuum tank, the second vacuum tank and the third vacuum tank, a first gas storage tank guide pipe, a second gas storage tank guide pipe and a third gas storage tank guide pipe which are respectively connected with the first vacuum tank guide pipe, the second vacuum tank guide pipe and the third vacuum tank guide pipe, a UF product water tank guide pipe which is respectively connected with the first PMUF product water pump, the second PMUF product water pump and the third PMUF product water pump, a first pump room drain pipe, a second pump room drain pipe and a third pump room drain pipe which are respectively connected with the first self-cleaning filter, the second self-cleaning filter and the third self-cleaning filter, and a UF backwash pump guide pipe which is respectively connected with the first membrane pool, the second membrane pool and the third membrane pool.
According to the technical scheme, the immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment further comprises a first auxiliary conduit, a second auxiliary conduit and a third auxiliary conduit, wherein the two ends of the first auxiliary conduit, the second auxiliary conduit and the third auxiliary conduit are respectively connected with the OTA water production pool water pipe, the first membrane pool conduit, the second membrane pool conduit and the third membrane pool conduit.
The immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment further comprises a clarification reaction tank conduit respectively connected with the first membrane tank, the second membrane tank and the third membrane tank, and a membrane tank continuous sludge discharge pump arranged on the clarification reaction tank conduit.
The immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment further comprises an auxiliary clarification reaction tank conduit with one end connected with the clarification reaction tank conduit, and a membrane tank emergency sludge discharge pump arranged on the auxiliary clarification reaction tank conduit.
The immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment further comprises a first oxidant dosing pipe, a second oxidant dosing pipe and a third oxidant dosing pipe which are respectively connected with the first membrane pool, the second membrane pool and the third membrane pool.
According to the technical scheme, the number of the membrane blocks in the first membrane pool, the number of the membrane blocks in the second membrane pool and the number of the membrane blocks in the third membrane pool are respectively three.
Compared with the prior art, the utility model discloses a be applied to phenol cyanogen waste water treatment's submergence formula ultrafiltration system's beneficial effect lies in: the device has reasonable design, can complete the efficient, safe and stable treatment of phenol-cyanogen wastewater, realizes the energy-saving, environment-friendly and safe wastewater treatment operation, and has strong practicability.
Drawings
FIG. 1 is a schematic structural diagram of an immersion type ultrafiltration system applied to phenol-cyanogen wastewater treatment of the present invention;
Detailed Description
The invention will be further elucidated with reference to the drawings and the specific embodiments.
Examples
An immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment as shown in fig. 1 comprises an OTA water production tank 1, a first self-cleaning filter 2, a second self-cleaning filter 3, a third self-cleaning filter 4, a first membrane tank 10, a second membrane tank 11, a third membrane tank 12, a first vacuum tank 13, a second vacuum tank 14, a third vacuum tank 15, a first water pump 41 for PMUF water production, a second water pump 42 for PMUF water production, and a third water pump 43 for PMUF water production; the OTA water producing pool 1 is provided with an inclined plate sedimentation water inlet pipe 9, an OTA water producing pool water pipe 8 respectively connected with the OTA water producing pool 1, a first self-cleaning filter 2, a second self-cleaning filter 3 and a third self-cleaning filter 4, a first PMUF raw water pump 16, a second PMUF raw water pump 17 and a third PMUF raw water pump 18 respectively arranged on the OTA water producing pool water pipe 8, a first membrane pool conduit 44, a second membrane pool conduit 45 and a third membrane pool conduit 46 respectively connected with the first self-cleaning filter 2, the second self-cleaning filter 3, the third self-cleaning filter 4, the first membrane pool 10, the second membrane pool 11 and the third membrane pool 12 at two ends, a blast pipe 39 respectively connected with the first membrane pool 10, the second membrane pool 11 and the third membrane pool 12, and a first membrane pool 10, the second membrane pool 11, the third membrane pool 12, a first vacuum tank 13, a second vacuum tank 14 and a first vacuum tank 15 respectively connected with the first membrane pool 10, the second membrane pool 11, the third vacuum tank 15, A second vacuum tank conduit 48, a third vacuum tank conduit 49, a first tap water replenishing pipe 29, a second tap water replenishing pipe 32, a third tap water replenishing pipe 35 respectively connected to the first vacuum tank 13, the second vacuum tank 14, the third vacuum tank 15, a first gas storage tank conduit 30, a second gas storage tank conduit 33 respectively connected to the first vacuum tank conduit 47, the second vacuum tank conduit 48, the third vacuum tank conduit 49, a third air storage tank conduit 36, a UF water production tank conduit 40 respectively connected with a first PMDUF water production pump 41, a second PMDUF water production pump 42 and a third PMDUF water production pump 43, a first pump room drain pipe 22, a second pump room drain pipe 23 and a third pump room drain pipe 24 respectively connected with a first self-cleaning filter 2, a second self-cleaning filter 3 and a third self-cleaning filter 4, and a UF backwashing pump conduit 38 respectively connected with the first membrane pool 10, the second membrane pool 11 and the third membrane pool 12.
Further preferably, the immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment further comprises a first auxiliary conduit 5, a second auxiliary conduit 6 and a third auxiliary conduit 7, wherein two ends of the first auxiliary conduit 5, the second auxiliary conduit 6 and the third auxiliary conduit 7 are respectively connected with the OTA water production pool water pipe 8, the first membrane pool conduit 44, the second membrane pool conduit 45 and the third membrane pool conduit 46; the immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment also comprises a clarification reaction tank conduit 19 which is respectively connected with the first membrane tank 10, the second membrane tank 11 and the third membrane tank 12, and a membrane tank continuous sludge discharge pump 21 which is arranged on the clarification reaction tank conduit 19; the immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment also comprises an auxiliary clarification reaction tank conduit 25 with one end connected with the clarification reaction tank conduit 19 and a membrane tank emergency sludge discharge pump 20 arranged on the auxiliary clarification reaction tank conduit 25; the immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment also comprises a first oxidant dosing pipe 31, a second oxidant dosing pipe 34 and a third oxidant dosing pipe 37 which are respectively connected with the first membrane pool 10, the second membrane pool 11 and the third membrane pool 12; and the number of the membrane blocks in the first membrane tank 10, the second membrane tank 11 and the third membrane tank 12 is respectively three.
The immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment has reasonable design, can complete the high-efficiency, safe and stable treatment of phenol-cyanogen wastewater, realizes the energy-saving, environment-friendly and safe wastewater treatment operation, and has strong practicability.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of modifications can be made without departing from the principle of the present invention, and these modifications should also be regarded as the protection scope of the present invention.
Claims (6)
1. The utility model provides an submergence formula ultrafiltration system for phenol cyanogen waste water treatment which characterized in that: the device comprises an OTA water production tank (1), a first self-cleaning filter (2), a second self-cleaning filter (3), a third self-cleaning filter (4), a first membrane pool (10), a second membrane pool (11), a third membrane pool (12), a first vacuum tank (13), a second vacuum tank (14), a third vacuum tank (15), a first PMUF water production pump (41), a second PMUF water production pump (42) and a third PMUF water production pump (43); an inclined plate sedimentation water inlet pipe (9), an OTA water production pool water pipe (8) respectively connected with the OTA water production pool (1), a first self-cleaning filter (2), a second self-cleaning filter (3) and a third self-cleaning filter (4), a first PMUF raw water pump (16), a second PMUF raw water pump (17) and a third PMUF raw water pump (18) respectively arranged on the OTA water production pool water pipe (8), a first membrane pool conduit (44), a second membrane pool conduit (45) and a third membrane pool conduit (46) respectively connected with the first self-cleaning filter (2), the second self-cleaning filter (3), the third self-cleaning filter (4), the first membrane pool (10), the second membrane pool (11) and the third membrane pool (12) at two ends, and a blast pipe (39) respectively connected with the first membrane pool (10), the second membrane pool (11) and the third membrane pool (12), a first vacuum tank conduit (47), a second vacuum tank conduit (48) and a third vacuum tank conduit (49) which are respectively connected with the first membrane pool (10), the second membrane pool (11), the third membrane pool (12), the first vacuum tank (13), the second vacuum tank (14) and the third vacuum tank (15), a first tap water replenishing pipe (29), a second tap water replenishing pipe (32) and a third tap water replenishing pipe (35) which are respectively connected with the first vacuum tank (13), the second vacuum tank (14) and the third vacuum tank (15), a first air storage tank conduit (30), a second air storage tank conduit (33) and a third air storage tank conduit (36) which are respectively connected with the first vacuum tank conduit (47), the second vacuum tank conduit (48) and the third vacuum tank conduit (49), and a water production pool conduit (40) which is respectively connected with the first PMUF water production pump (41), the second PMUF water production pump (42) and the third PMUF water production pump (43), and a first pump room drain pipe (22), a second pump room drain pipe (23) and a third pump room drain pipe (24) which are respectively connected with the first self-cleaning filter (2), the second self-cleaning filter (3) and the third self-cleaning filter (4), and a UF backwashing pump guide pipe (38) which is respectively connected with the first membrane pool (10), the second membrane pool (11) and the third membrane pool (12).
2. The submerged ultrafiltration system for phenol-cyanogen wastewater treatment according to claim 1, wherein: be applied to submergence formula ultrafiltration system of phenol cyanogen waste water treatment still includes first auxiliary conduit (5), second auxiliary conduit (6), third auxiliary conduit (7) that both ends are connected with OTA product water pond water pipe (8), first membrane pond pipe (44), second membrane pond pipe (45), third membrane pond pipe (46) respectively.
3. The submerged ultrafiltration system for phenol-cyanogen wastewater treatment according to claim 2, wherein: the immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment further comprises a clarification reaction tank conduit (19) respectively connected with the first membrane tank (10), the second membrane tank (11) and the third membrane tank (12), and a membrane tank continuous sludge discharge pump (21) arranged on the clarification reaction tank conduit (19).
4. The submerged ultrafiltration system for phenol-cyanogen wastewater treatment according to claim 3, wherein: be applied to submergence formula ultrafiltration system of phenol cyanogen waste water treatment, still include supplementary clarification reaction tank pipe (25) that one end and clarification reaction tank pipe (19) are connected to and set up membrane pool emergency sludge pump (20) on supplementary clarification reaction tank pipe (25).
5. The submerged ultrafiltration system for phenol-cyanogen wastewater treatment according to claim 4, wherein: the immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment further comprises a first oxidant dosing pipe (31), a second oxidant dosing pipe (34) and a third oxidant dosing pipe (37) which are respectively connected with the first membrane pool (10), the second membrane pool (11) and the third membrane pool (12).
6. The submerged ultrafiltration system for phenol-cyanogen wastewater treatment according to claim 5, wherein: the number of the membrane blocks in the first membrane pool (10), the second membrane pool (11) and the third membrane pool (12) is three.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022352237.XU CN213680155U (en) | 2020-10-21 | 2020-10-21 | Immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022352237.XU CN213680155U (en) | 2020-10-21 | 2020-10-21 | Immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment |
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| Publication Number | Publication Date |
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| CN213680155U true CN213680155U (en) | 2021-07-13 |
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| CN202022352237.XU Active CN213680155U (en) | 2020-10-21 | 2020-10-21 | Immersed ultrafiltration system applied to phenol-cyanogen wastewater treatment |
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