CN205329026U - Branch sieve system is reinforceed to biological enzyme preparation - Google Patents
Branch sieve system is reinforceed to biological enzyme preparation Download PDFInfo
- Publication number
- CN205329026U CN205329026U CN201521144202.XU CN201521144202U CN205329026U CN 205329026 U CN205329026 U CN 205329026U CN 201521144202 U CN201521144202 U CN 201521144202U CN 205329026 U CN205329026 U CN 205329026U
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- pump
- electromagnetic valve
- biological enzyme
- nutrition
- screening system
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Abstract
The utility model discloses a branch sieve system is reinforceed to biological enzyme preparation, its characterized in that: divide the screen pipe way and divide the biochemical pond of sieving the tube coupling with the front end including the front end, biochemical pond includes a plurality of cell bodies, bottom support and a plurality of heel brace, and a plurality of cell body settings are on the support of bottom, and the bottom support sets up on a plurality of heel braces. The utility model discloses can cultivate the oxygen microorganism, facultative microorganism and anaerobic microorganisms, the kind is more, divide the sieve can obtain advantage microflora and biological enzyme through reinforceing, the degree that becomes more meticulous height, product quality is good, improves its treatment effect greatly, the biochemical treatment effect can improve more than 30%, if be used for the biochemical debugging initial stage then can correspondingly shorten its debug time, catalysis efficiency is higher.
Description
Technical field
This utility model relates to technical field of sewage, particularly relates to a kind of biological enzyme formulation strengthening screening system。
Background technology
Development along with modern compound probability, a large amount of difficult degradation macromolecule organics enter in various workers and peasants' waste water and urban comprehensive wastewater, owing to itself having structural complexity and refractory organics, it is accordingly difficult to be aoxidized by the microbial decomposition in conventional biological treatment system at short notice so that the adaptability that the time increases significantly, waste water is changed by biochemical system of biochemical treatment of wastewater startup at present is substantially reduced。It addition, because microorganism has multiformity, enzyme preparation has specificity, will select suitable microorganism and enzyme preparation is comparatively difficult and complicated work。In order to solve this problem, artificial pressure is taked to add high-effective microorganism and specific enzyme preparation, the problem that difficult degradation macromolecule microorganism difficulty drops can be efficiently solved, greatly add again sewage disposal system stability and resistance to impact simultaneously, but there is presently no the technology of a kind of complete mature realizing this effect。
Utility model content
Because the drawbacks described above of prior art, technical problem to be solved in the utility model is to provide a kind of biological enzyme formulation strengthening screening system, employing is taken from nature and is used for natural principle, turn out safety non-toxic, efficient microorganism and enzyme preparation, the clearance improving COD, BOD5, TOC, ammonia nitrogen, total phosphorus, colourity, turbidity and some specific hard-degraded substance that can be bigger, use water colorless, non-foam, as clear as crystal, efficiently solve the deficiencies in the prior art。
For achieving the above object, this utility model provides a kind of biological enzyme formulation strengthening screening system, it is characterised in that: include front end sub-sieve pipeline and the biochemistry pool being connected with front end sub-sieve pipeline;Described front end sub-sieve pipeline includes fluid reservoir TK1 and transition tank TK2, described fluid reservoir TK1 has three intake lines, wherein the first intake line is connected with intake pump PD1 by entering water electromagnetic valve YV1, second intake line is connected with air intake pump KY1 by air inlet electromagnetic valve YV8,3rd intake line adds entering water electromagnetic valve YV6 by nutrition and adds pump PD5 with nutrition and be connected, and described nutrition adds pump PD5 and is connected with nutrient tank TK3;Described fluid reservoir TK1 has two output pipes, and wherein the first output pipe passes sequentially through and strains bacterium pump PD2, strains bacterium electromagnetic valve YV2 and be connected with transition tank TK2, and the second output pipe is connected with sludge pump PD4 by soil discharging electromagnetic valve YV4;Described transition tank TK2 input adds entering water electromagnetic valve YV7 by nutrition and adds pump PD6 with nutrition and be connected, described nutrition adds pump PD6 and is connected with nutrient tank TK4, mono-outfan of described transition tank TK2 is connected to biochemistry pool by draining pump PD3, drain solenoid valve YV3, and described another outfan of transition tank TK2 is connected to biochemistry pool by soil discharging electromagnetic valve YV5, sludge pump PD4;Described biochemistry pool includes multiple cell body, bottom bracket and multiple heel brace, and the plurality of cell body is arranged on bottom bracket, and described bottom bracket is arranged on multiple heel brace。
Further, described fluid reservoir TK1 and transition tank TK2 top are respectively arranged with liquid level control switch LT1, LT2。
Further, described soil discharging electromagnetic valve YV4, soil discharging electromagnetic valve YV5 outfan import a road pipeline, be then attached to sludge pump PD4。
Further, described transition tank TK2 is additionally provided with diving circulating pump PD7。
Further, described cell body has eight, and four is one group, and every packet size is identical, and often group internal structure is different。
Further, described heel brace has nine, is separately positioned on each node place of rectangle steel of welding heel brace。
Further, described bottom bracket uses angle bar to be welded。
The beneficial effects of the utility model are:
1, this utility model can cultivate aerobic microbiological, aerobic-anaerobic microbe and anaerobe, and kind is more;
2, this utility model can cultivate the microbiologic population of various kind, is cultivated by the operation of ER system, it is possible to obtain superior microorganism group, and enzyme, and from being strengthened sub-sieve, good product quality;
3, this utility model is according to the process requirement processing different waste water, designs different system in combination, thus obtaining variable concentrations, different types of microorganism and enzyme thereof, and strengthened sub-sieve, in the middle of sewage disposal, the degree that becomes more meticulous height, is greatly improved its treatment effect;
4, this utility model is used in the middle of each biochemical sewage treatment facility by the enzyme of biological enzyme formulation strengthening screening system gained, make Biochemical Treatment can improve more than 30%, if for the biochemical debugging initial stage, can shorten its debugging time accordingly, catalytic efficiency is higher。
Below with reference to accompanying drawing, the technique effect of design of the present utility model, concrete structure and generation is described further, to be fully understood from the purpose of this utility model, feature and effect。
Accompanying drawing explanation
Fig. 1 is biochemistry pool structural representation of the present utility model;
Fig. 2 is front end of the present utility model sub-sieve pipeline structure schematic diagram。
Detailed description of the invention
As shown in Figure 1, 2, a kind of biological enzyme formulation strengthening screening system, it is characterised in that: include front end sub-sieve pipeline and the biochemistry pool being connected with front end sub-sieve pipeline;Described front end sub-sieve pipeline includes fluid reservoir TK1 and transition tank TK2, described fluid reservoir TK1 has three intake lines, wherein the first intake line is connected with intake pump PD1 by entering water electromagnetic valve YV1, second intake line is connected with air intake pump KY1 by air inlet electromagnetic valve YV8,3rd intake line adds entering water electromagnetic valve YV6 by nutrition and adds pump PD5 with nutrition and be connected, and described nutrition adds pump PD5 and is connected with nutrient tank TK3;Described fluid reservoir TK1 has two output pipes, and wherein the first output pipe passes sequentially through and strains bacterium pump PD2, strains bacterium electromagnetic valve YV2 and be connected with transition tank TK2, and the second output pipe is connected with sludge pump PD4 by soil discharging electromagnetic valve YV4;Described transition tank TK2 input adds entering water electromagnetic valve YV7 by nutrition and adds pump PD6 with nutrition and be connected, described nutrition adds pump PD6 and is connected with nutrient tank TK4, mono-outfan of described transition tank TK2 is connected to biochemistry pool by draining pump PD3, drain solenoid valve YV3, and described another outfan of transition tank TK2 is connected to biochemistry pool by soil discharging electromagnetic valve YV5, sludge pump PD4;Described biochemistry pool includes multiple cell body 1, bottom bracket 3 and multiple heel brace 4, and the plurality of cell body 1 is arranged on bottom bracket 3, and described bottom bracket 3 is arranged on multiple heel brace 4。
It is preferred that described fluid reservoir TK1 and transition tank TK2 top are respectively arranged with liquid level control switch LT1, LT2。
It is preferred that the outfan of described soil discharging electromagnetic valve YV4, soil discharging electromagnetic valve YV5 imports a road pipeline, it is then attached to sludge pump PD4。
It is preferred that described transition tank TK2 is additionally provided with diving circulating pump PD7。
It is preferred that described cell body 1 has eight, four is one group, and every packet size is identical, and often group internal structure is different。
It is preferred that described heel brace 4 has nine, it is separately positioned on each node place of rectangle steel of welding heel brace 4。
It is preferred that described bottom bracket 3 uses angle bar to be welded。
Front end of the present utility model sub-sieve pipeline operation principle is:
1, water inlet controls to illustrate:
Non-follow control, entering water electromagnetic valve YV1 and intake pump PD1 can manual unlocking。
Automatically control, when TK1 liquid level control switch LT1 is in low liquid level, automatically turn on intake pump PD1 and entering water electromagnetic valve YV1, when liquidometer is in high liquid level, close intake pump PD1 and entering water electromagnetic valve YV1。
2, TK1 runs and controls to illustrate:
Non-follow control, can manually control air inlet electromagnetic valve YV8, strains bacterium pump PD2, strains bacterium electromagnetic valve YV2。
Automatically control, when TK1 water inlet is in high liquid level, automatically turn on air inlet electromagnetic valve YV8, run 3 hours (time is adjustable) and stop air inlet electromagnetic valve 2 hours (time is adjustable), it is then turned on air inlet electromagnetic valve YV8 and runs 1 hour (time is adjustable), after stopping 1 hour (time is adjustable) again, bacterium pump PD2 is strained in unlatching, strain bacterium electromagnetic valve YV2 (to note: now in TK2, LT2 is in low liquid level, if now in TK2, LT2 is in high liquid level, PD2, YV2 does not start and sends alarm and notifies that operator check the level condition (low liquid level startup) of TK2 in time, when in TK2, liquidometer LT2 is in low liquid level again, sound all clear and start PD2, YV2);When LT2 is in high liquid level in TK2 or when LT1 is in low liquid level in TK1, closes and strain bacterium pump PD2, strain bacterium electromagnetic valve YV2 (such TK1 complete 1 cycle repeat above-mentioned 1-2 point) in (estimating 8 hours to be 1 cycle) the 2nd cycle。
3, TK2 runs system explanation:
Non-follow control, Non-follow control diving circulating pump PD7, draining pump PD3, drain solenoid valve YV3。
Automatically control, when TK2 water inlet is in high liquid level, after automatically turning on diving circulating pump PD7 operation 5.5 hours (time is adjustable) 1 hour out of service (time is adjustable), opening water discharge pump PD3, drain solenoid valve YV3, when the LT2 liquidometer in TK2 is in low liquid level, second round (note: TK2 is the transition tank of TK1, and TK2 cycle computation time is in high liquid level based on the LT2 in TK2) is reentered after closing draining pump PD3, drain solenoid valve YV3。
4, other Non-follow control: nutrition adds pump PD5, nutrition adds entering water electromagnetic valve YV6, to add entering water electromagnetic valve YV7, TK1 soil discharging electromagnetic valve YV4, TK2 soil discharging electromagnetic valve YV5 and sludge pump PD4 be Non-follow control in nutrition, does not set and automatically controls。
Nutritional solution after front end sub-sieve pipeline processes finally flows into each cell body of biochemistry pool and carries out biochemical reaction, obtains wide variety, biological enzyme formulation that concentration is different。
Preferred embodiment of the present utility model described in detail above。Should be appreciated that those of ordinary skill in the art just can make many modifications and variations according to design of the present utility model without creative work。Therefore, all technical staff in the art pass through the available technical scheme of logical analysis, reasoning, or a limited experiment on the basis of existing technology according to design of the present utility model, all should in the protection domain being defined in the patent claims。
Claims (7)
1. a biological enzyme formulation strengthening screening system, it is characterised in that: include front end sub-sieve pipeline and the biochemistry pool being connected with front end sub-sieve pipeline;Described front end sub-sieve pipeline includes fluid reservoir TK1 and transition tank TK2, described fluid reservoir TK1 has three intake lines, wherein the first intake line is connected with intake pump PD1 by entering water electromagnetic valve YV1, second intake line is connected with air intake pump KY1 by air inlet electromagnetic valve YV8,3rd intake line adds entering water electromagnetic valve YV6 by nutrition and adds pump PD5 with nutrition and be connected, and described nutrition adds pump PD5 and is connected with nutrient tank TK3;Described fluid reservoir TK1 has two output pipes, and wherein the first output pipe passes sequentially through and strains bacterium pump PD2, strains bacterium electromagnetic valve YV2 and be connected with transition tank TK2, and the second output pipe is connected with sludge pump PD4 by soil discharging electromagnetic valve YV4;Described transition tank TK2 input adds entering water electromagnetic valve YV7 by nutrition and adds pump PD6 with nutrition and be connected, described nutrition adds pump PD6 and is connected with nutrient tank TK4, mono-outfan of described transition tank TK2 is connected to biochemistry pool by draining pump PD3, drain solenoid valve YV3, and described another outfan of transition tank TK2 is connected to biochemistry pool by soil discharging electromagnetic valve YV5, sludge pump PD4;Described biochemistry pool includes multiple cell body (1), bottom bracket (3) and multiple heel brace (4), and the plurality of cell body (1) is arranged on bottom bracket (3), and described bottom bracket (3) is arranged on multiple heel brace (4)。
2. a kind of biological enzyme formulation strengthening screening system as claimed in claim 1, it is characterised in that: described fluid reservoir TK1 and transition tank TK2 top are respectively arranged with liquid level control switch LT1, LT2。
3. biological enzyme formulation strengthening screening system as claimed in claim 1 a kind of, it is characterised in that: described soil discharging electromagnetic valve YV4, soil discharging electromagnetic valve YV5 outfan import a road pipeline, be then attached to sludge pump PD4。
4. a kind of biological enzyme formulation strengthening screening system as claimed in claim 1, it is characterised in that: described transition tank TK2 is additionally provided with diving circulating pump PD7。
5. a kind of biological enzyme formulation strengthening screening system as claimed in claim 1, it is characterised in that: described cell body (1) has eight, and four is one group, and every packet size is identical, and often group internal structure is different。
6. a kind of biological enzyme formulation strengthening screening system as claimed in claim 1, it is characterised in that: described heel brace (4) has nine, is separately positioned on each node place of rectangle steel of welding heel brace (4)。
7. a kind of biological enzyme formulation strengthening screening system as claimed in claim 1, it is characterised in that: described bottom bracket (3) uses angle bar to be welded。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201521144202.XU CN205329026U (en) | 2015-12-31 | 2015-12-31 | Branch sieve system is reinforceed to biological enzyme preparation |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201521144202.XU CN205329026U (en) | 2015-12-31 | 2015-12-31 | Branch sieve system is reinforceed to biological enzyme preparation |
Publications (1)
Publication Number | Publication Date |
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CN205329026U true CN205329026U (en) | 2016-06-22 |
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Family Applications (1)
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CN201521144202.XU Expired - Fee Related CN205329026U (en) | 2015-12-31 | 2015-12-31 | Branch sieve system is reinforceed to biological enzyme preparation |
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CN (1) | CN205329026U (en) |
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2015
- 2015-12-31 CN CN201521144202.XU patent/CN205329026U/en not_active Expired - Fee Related
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Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160622 Termination date: 20161231 |