Background
The activated sludge process is an aerobic biological treatment method for sewage, and nowadays, the activated sludge process and a derivative and improvement process thereof are the most widely used methods for treating urban sewage. It can remove soluble and colloidal biochemical organic substances, suspended solids and other substances adsorbed by activated sludge from sewage, and can remove a part of phosphorus and nitrogen. The activated sludge process is a main method for biologically treating wastewater mainly containing activated sludge. When the water temperature of the pool is about 30 ℃, the activity of the activated sludge is strongest, the sewage treatment effect is good, the metabolism capability of aerobic organisms is reduced at the temperature of less than 20 ℃ or more than 40 ℃, and the sewage treatment capability is reduced. Water cooling towers are generally built in sewage treatment plants, and when the water temperature is high in summer, the water cooling towers are put into use, so that the water temperature of a water pool is easy to control. However, in winter, the temperature of the water coming from each channel is lower, the water temperature is further reduced after passing through each water tank, and when the water flows into the oxidation tank, the water temperature is relatively lower, so that the metabolism capability of aerobic organisms is influenced, and the sewage treatment effect is not ideal. If heat exchange equipment is additionally arranged before the incoming water enters the aerobic biological water tank to improve the water temperature, the utilization rate of the equipment is not high (the equipment is operated only when the water is cold in winter), and the sewage operation cost is increased.
Disclosure of Invention
The utility model aims at providing a portable oxidation pond temperature rising device that intakes to the above-mentioned defect that prior art exists, when keeping pond temperature about 30 ℃, make activated sludge's activity strongest, sewage treatment is effectual.
The technical scheme is as follows: the device comprises an oxidation pond (1), a steam conveying rubber tube (2), an oxidation pond water inlet mixing tank (3), an oxidation pond water inlet pipe (4) and a temperature rising device (5), wherein the oxidation pond water inlet mixing tank (3) is integrally arranged at the upper part of one side of the oxidation pond (1), the oxidation pond water inlet mixing tank (3) is connected with the oxidation pond water inlet pipe (4), the temperature rising device (5) is arranged in the oxidation pond water inlet pipe (4), and the steam conveying rubber tube (2) penetrates through the oxidation pond water inlet mixing tank (3) and is connected to the temperature rising device (5); the temperature rising device (5) comprises a steam connecting pipe (5.1), a cylindrical temperature rising device body (5.3) and a steam diverging hole (5.4), the inside of the temperature rising device body (5.3) is hollow, the steam connecting pipe (5.1) is integrally arranged at the center of the top of the temperature rising device body (5.3), the steam connecting pipe (5.1) is connected with a steam conveying rubber pipe (2), and the steam diverging hole (5.4) is formed in the outer wall of the temperature rising device body (5.3).
Preferably, the oxidation pond inlet pipe 4 comprises a bent pipe section and a vertical section, the temperature rising device (5) is placed at the vertical section of the oxidation pond inlet pipe 4, and the bent pipe section is connected with the oxidation pond inlet water mixing tank (3).
Preferably, two fixing rings (5.2) are welded on the top circumference of the warmer body (5.3).
Preferably, two fixing rings (5.2) on the warmer body (5.3) are symmetrically arranged.
Preferably, the iron wire penetrates through the fixing ring (5.2) and is wound at the joint of the steam connecting pipe (5.1) and the steam conveying rubber pipe (2), so that the steam conveying rubber pipe (2) is firmly fixed with the temperature rising device (5).
Preferably, the steam diverging holes (5.4) are evenly distributed on the outer wall of the warmer body (5.3).
The utility model has the advantages that: the utility model discloses keep pond temperature when about 30 ℃, make activated sludge's activity strongest, sewage treatment is effectual, the utility model discloses a place intensification ware in oxidation pond inlet pipe to let in steam, thereby improved oxidation pond inlet water temperature, and this intensification ware simple manufacture, simple to operate follow-up and take, the cost is lower.
Detailed Description
The preferred embodiments of the present invention will be described in conjunction with the accompanying drawings, and it will be understood that they are presented herein only to illustrate and explain the present invention, and not to limit the present invention.
Example 1:
as shown in fig. 1, the utility model comprises an oxidation pond 1, a steam conveying rubber tube 2, an oxidation pond water inlet mixing tank 3, an oxidation pond water inlet pipe 4 and a temperature rising device 5, wherein the oxidation pond water inlet mixing tank 3 is arranged at the upper part of one side of the oxidation pond 1, the oxidation pond 1 and the oxidation pond water inlet mixing tank 3 are integrally arranged, the oxidation pond 1 is communicated with the oxidation pond water inlet mixing tank 3, the oxidation pond water inlet mixing tank 3 is connected with the oxidation pond water inlet pipe 4, the temperature rising device 5 is arranged in the oxidation pond water inlet pipe 4, and the steam conveying rubber tube 2 passes through the oxidation pond water inlet mixing tank 3 from the oxidation pond 1 and is connected with the temperature rising device 5; the temperature rising device 5 comprises a steam connecting pipe 5.1, a cylindrical temperature rising device body 5.3 and a steam diverging hole 5.4, the inside of the temperature rising device body 5.3 is hollow, the steam connecting pipe 5.1 is integrally arranged at the center of the top of the temperature rising device body 5.3, the steam connecting pipe 5.1 is connected with a steam conveying rubber pipe 2, the steam diverging hole 5.4 is formed in the outer wall of the temperature rising device body 5.3, the effluent of the secondary sedimentation tank flows into an oxidation tank water inlet mixing tank 3 through an oxidation tank water inlet pipe 4, the steam conveying rubber pipe 2 is connected with the temperature rising device steam connecting pipe 5.1, and the conveyed steam is diverged out through the steam diverging hole 5.4 and is fully mixed with the incoming water.
Referring to fig. 2, the oxidation pond water inlet pipe 4 comprises a bent pipe section 4.1 and a vertical section 4.2, the temperature rising device 5 is arranged on the vertical section 4.2 of the oxidation pond water inlet pipe 4, and the bent pipe section 4.1 is connected with the oxidation pond water inlet mixing tank 3.
As shown in fig. 3, two fixing rings 5.2 are welded on the top circumference of the warmer body 5.3, the two fixing rings 5.2 on the warmer body 5.3 are symmetrically arranged, and the iron wire penetrates through the fixing rings 5.2 and is wound at the joint of the steam connecting pipe 5.1 and the steam conveying rubber pipe 2, so that the steam conveying rubber pipe 2 and the warmer 5 are firmly fixed.
The iron wire penetrates through the fixing ring 5.2 and is wound at the joint of the steam connecting pipe 5.1 and the steam conveying rubber pipe 2, so that the steam conveying rubber pipe 2 and the temperature rising device 5 are firmly fixed, and the steam conveying rubber pipe 2 is prevented from being separated from the steam connecting pipe 5.1 under the condition of long-time pressure.
In addition, the steam divergence holes 5.4 are uniformly distributed on the outer wall of the temperature rising device body 5.3, and 3, the steam and the water are uniformly mixed.
The effluent of the secondary sedimentation tank flows into the oxidation tank water inlet mixing tank 3 through the oxidation tank water inlet pipe 4, and the temperature rising device 5 is arranged in the vertical section 4.2 of the oxidation tank water inlet pipe 4 for ensuring that the steam heat is fully absorbed. The steam conveying rubber tube 2 is connected with a steam connecting tube 5.1 of the temperature rising device, the steam conveying rubber tube 2 is firmly fixed with the temperature rising device through a fixing ring 5.2 by using an iron wire, and steam conveyed by the steam conveying rubber tube 2 is diffused out through a steam diffusing hole 5.4 and is fully mixed with incoming water. The water temperature of the oxidation pond is controlled by controlling the amount of the introduced steam.
The utility model discloses keep pond temperature when about 30 ℃, make activated sludge's activity strongest, sewage treatment is effectual, the utility model discloses a place intensification ware in oxidation pond inlet pipe to let in steam, thereby improved oxidation pond inlet water temperature, and this intensification ware simple manufacture, simple to operate follow-up and take, the cost is lower.
Example 2:
the utility model discloses an oxidation pond 1, steam transport rubber tube 2, oxidation pond mixing tank 3 that intakes, oxidation pond inlet tube 4, intensifiers 5, one side upper portion of oxidation pond 1 is equipped with oxidation pond mixing tank 3 that intakes, oxidation pond 1 and oxidation pond mixing tank 3 integrative settings that intakes, oxidation pond 1 and oxidation pond mixing tank 3 intercommunication that intakes, oxidation pond mixing tank 3 that intakes connects oxidation pond inlet tube 4, be equipped with intensifiers 5 in the oxidation pond inlet tube 4, steam transport rubber tube 2 passes oxidation pond mixing tank 3 that intakes from oxidation pond 1 and is connected to intensifiers 5; the temperature rising device 5 comprises a steam connecting pipe 5.1, a cylindrical temperature rising device body 5.3 and a steam diverging hole 5.4, the inside of the temperature rising device body 5.3 is hollow, the steam connecting pipe 5.1 is integrally arranged at the center of the top of the temperature rising device body 5.3, the steam connecting pipe 5.1 is connected with a steam conveying rubber pipe 2, the steam diverging hole 5.4 is formed in the outer wall of the temperature rising device body 5.3, the effluent of the secondary sedimentation tank flows into an oxidation tank water inlet mixing tank 3 through an oxidation tank water inlet pipe 4, the steam conveying rubber pipe 2 is connected with the temperature rising device steam connecting pipe 5.1, and the conveyed steam is diverged out through the steam diverging hole 5.4 and is fully mixed with the incoming water.
Referring to fig. 2, the oxidation pond water inlet pipe 4 comprises a bent pipe section 4.1 and a vertical section 4.2, the temperature rising device 5 is arranged on the vertical section 4.2 of the oxidation pond water inlet pipe 4, and the bent pipe section 4.1 is connected with the oxidation pond water inlet mixing tank 3.
As shown in fig. 3, two fixing rings 5.2 are welded on the top circumference of the warmer body 5.3, the two fixing rings 5.2 on the warmer body 5.3 are symmetrically arranged, and the iron wire penetrates through the fixing rings 5.2 and is wound at the joint of the steam connecting pipe 5.1 and the steam conveying rubber pipe 2, so that the steam conveying rubber pipe 2 and the warmer 5 are firmly fixed.
The iron wire penetrates through the fixing ring 5.2 and is wound at the joint of the steam connecting pipe 5.1 and the steam conveying rubber pipe 2, so that the steam conveying rubber pipe 2 and the temperature rising device 5 are firmly fixed, and the steam conveying rubber pipe 2 is prevented from being separated from the steam connecting pipe 5.1 under the condition of long-time pressure.
In addition, the steam divergence holes 5.4 are uniformly distributed on the outer wall of the temperature rising device body 5.3, and 3, the steam and the water are uniformly mixed.
The difference from the embodiment 1 is that:
as shown in fig. 4, a temperature sensor 6 is arranged in an oxidation pond 1, an electromagnetic valve 7 is arranged on a steam conveying rubber pipe 2, the temperature sensor 6 is connected to a controller 8, the controller 8 is arranged on the outer wall of the oxidation pond 1 and can be fixed by welding, the electromagnetic valve 7 is connected to the controller 8, a set temperature is input into the controller 8 by 30 degrees and is higher than 30 degrees, the electromagnetic valve 7 is controlled to be turned off, the input of steam is reduced and is lower than 30 degrees, the electromagnetic valve 7 is controlled to be turned on and is turned off to increase the input of steam, the water temperature of the oxidation pond is controlled by controlling the amount of the introduced steam, the water temperature of the water pond is kept at about 30 ℃, the activity of activated sludge is.
The effluent of the secondary sedimentation tank flows into the oxidation tank water inlet mixing tank 3 through the oxidation tank water inlet pipe 4, and the temperature rising device 5 is arranged in the vertical section 4.2 of the oxidation tank water inlet pipe 4 for ensuring that the steam heat is fully absorbed. The steam conveying rubber tube 2 is connected with a steam connecting tube 5.1 of the temperature rising device, the steam conveying rubber tube 2 is firmly fixed with the temperature rising device through a fixing ring 5.2 by using an iron wire, and steam conveyed by the steam conveying rubber tube 2 is diffused out through a steam diffusing hole 5.4 and is fully mixed with incoming water. The set temperature is input into the controller 8 to be 30 ℃ higher than 30 ℃, the electromagnetic valve 7 is controlled to be closed to reduce the input of steam, the temperature is lower than 30 ℃, the electromagnetic valve 7 is controlled to be opened to increase the input of steam, the water temperature of the oxidation pond is controlled by controlling the amount of the introduced steam, the water temperature of the oxidation pond is kept at about 30 ℃, the activity of activated sludge is strongest, and the sewage treatment effect is good.
The utility model discloses keep pond temperature when about 30 ℃, make activated sludge's activity strongest, sewage treatment is effectual, the utility model discloses a place the intensification ware in oxidation pond inlet pipe to let in steam, thereby improved oxidation pond inlet water temperature, and this intensification ware simple manufacture, simple to operate, the random access, the cost is lower, and the volume that lets in steam through controller control controls the oxidation pond temperature, keeps the pond temperature about 30 ℃, makes activated sludge's activity strongest, and sewage treatment is effectual.
The above description is only a preferred embodiment of the present invention, and any person skilled in the art may modify the present invention or modify it into an equivalent technical solution by using the technical solutions described above. Therefore, any simple modifications or equivalent replacements made according to the technical solution of the present invention belong to the scope of the claimed invention as far as possible.