CN102583440B - Water replenishing device of synthetic ammonia circulating water system and water replenishing method - Google Patents
Water replenishing device of synthetic ammonia circulating water system and water replenishing method Download PDFInfo
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- CN102583440B CN102583440B CN201210058394.7A CN201210058394A CN102583440B CN 102583440 B CN102583440 B CN 102583440B CN 201210058394 A CN201210058394 A CN 201210058394A CN 102583440 B CN102583440 B CN 102583440B
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Abstract
The invention belongs to the field of water replenishing of a synthetic ammonia circulating water system, and particularly relates to a water replenishing device of the synthetic ammonia circulating water system, which has the advantages of simple structure, stable operation, low cost and capabilities of reducing sewage discharge and avoiding environmental pollution, and a water replenishing method. The water replenishing device comprises the synthetic ammonia circulating system, wherein a water outlet of the synthetic ammonia circulating system is connected with a first valve, a first circulating water pump, a second valve, a water utilization organization, a third valve, a second circulating water pump, a fourth valve and a fifth valve in sequence; the fifth valve is connected with a water inlet of the synthetic ammonia circulating system through a pipeline; the synthetic ammonia circulating system is provided with a primary water replenishing port and a soft water replenishing port; the primary water replenishing port is connected with a primary water self-adjusting valve, a primary water flow meter and a primary water tank in sequence; and the soft water replenishing port is connected with a soft water self-adjusting valve, a soft water flow meter and a soft water tank in sequence. The water replenishing device has the advantages of simple structure, stable operation, low cost and capabilities of reducing sewage discharge and avoiding environmental pollution.
Description
Technical field
The invention belongs to synthetic ammonia circulating water system moisturizing field, be specifically related to a kind of simple in structurely, stable, with low cost, reduce quantity of wastewater effluent and synthetic ammonia circulating water system water replanishing device and method for supplementing water free from environmental pollution.
Background technology
Synthetic ammonia circulating water system moisturizing is at present mainly carried out supply by a water, and after 3-5 doubly concentrates, in circulating water system, every technic index exceeds standard, and must pass through the circulating water system blowdown and supplement in a large number the fresh water displacement, carrys out controlled circulation water water quality.Like this, not only water loss increases greatly, and in recirculated water, various medicaments run off simultaneously, have caused huge financial loss, have also increased the weight of production load and the contaminate environment of sewage works.
Summary of the invention
The object of the invention is to overcome defect of the prior art and provide a kind of simple in structure, stable, with low cost, reduce quantity of wastewater effluent and synthetic ammonia circulating water system water replanishing device and method for supplementing water free from environmental pollution.
The object of the present invention is achieved like this: the water outlet that the present invention includes synthetic ammonia circulating water system, described synthetic ammonia circulating water system by pipeline with the first valve, the first water circulating pump, the second valve, water unit, the 3rd valve, the second water circulating pump, the 4th valve and the 5th valve, be connected successively, described the 5th valve is connected with the water-in of synthetic ammonia circulating water system by pipeline, is respectively arranged with water water supplement port and additional soft wa ter mouth on described synthetic ammonia circulating water system; A described water water supplement port by pipeline successively with a water self-regulated valve, No. one time water ga(u)ge is connected with a water tank, described additional soft wa ter mouth pass through pipeline successively with soft water self-regulated valve, the soft water under meter is connected with the soft water water tank; Be provided with the first threeway between described the second water circulating pump and the 4th valve, one end of described threeway by pipeline successively with the 6th valve, sand-bed filter is connected with the 7th valve, be provided with the second threeway between described the 4th valve and the 5th valve, described the 7th valve is connected with an end of the second threeway by pipeline; The blow-off line of described sand-bed filter is connected with intermediate water reuse system with the 8th valve successively; Be provided with on-line monitoring system between described the 5th valve and synthetic ammonia circulating water system, described on-line monitoring system, one time water self-regulated valve is connected with turn-key system respectively with soft water self-regulated valve.
Method for supplementing water of the present invention, its step is as follows:
One, detect circulating water quality and the water yield in the synthetic ammonia circulating water system by on-line monitoring system, and data are sent in turn-key system;
Two, turn-key system calculates the cycles of concentration of recirculated water according to the data that transmit in step 1;
Three, the ratio that turn-key system is controlled soft water self-regulated valve and a water self-regulated valve by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Synthetic ammonia concentration multiple of circulating water system of the present invention is controlled at 3-5, and all kinds of water forms in accounting for circulating water system global cycle amount ratio: soft water 6 ‰-14.4 ‰, the ratio that now a corresponding water magnitude of recruitment accounts for internal circulating load is 14.4 ‰-3.5 ‰.When cycles of concentration is 3, when temperature is 0 ℃, the soft water minimum proportion is 6 ‰ of systemic circulation amount, and now a corresponding water yield is 9 ‰ of systemic circulation amount.When cycles of concentration is 3, when temperature is 40 ℃, the soft water minimum proportion is 9.6 ‰ of systemic circulation amount, and now a corresponding water yield is 14.4 ‰.When cycles of concentration is 4, when temperature is 40 ℃, the soft water minimum proportion is 12.8 ‰ of systemic circulation amount, and now a corresponding water yield is 8.5 ‰.When cycles of concentration is 5, when temperature is 0 ℃, the internal circulating load 9 ‰ that the soft water minimum proportion is system, now a corresponding water yield is 3.5 ‰.When cycles of concentration is 5, when temperature is 40 ℃, the soft water minimum proportion is 14.4 ‰ of systemic circulation amount, and now a corresponding water yield is 5.6 ‰.
The present invention does not need to increase other treatment facilities in the process of using, the corresponding water of configuration and soft water pipeline on the basis of original system, and self-regulated valve and under meter, by controlling the rational proportion of water and soft water, can realize.
On-line detecting system of the present invention detects the situation of circulating water quality and the water yield automatically, and information is passed to turn-key system, turn-key system carries out the automatic calculating of recirculated water cycles of concentration according to the circulating water quality situation received, provide an optimum water and additional soft wa ter ratio, and the self-regulated valve of controlling water and soft water system proportionally carries out moisturizing; Water and soft water are automatically controlled and are entered the synthetic ammonia circulating water system and advanced the water supply by turn-key system, to guarantee the recirculated water overall water quality, reach requirement; Recirculated water after water and additional soft wa ter directly enters water unit through the first water circulating pump, water unit's water out is divided into two parts after the second water circulating pump, a part is approximately 90% without sand-bed filter, a part ofly in addition approximately 10% enter sand-bed filter, recirculated water after sand-bed filter filters converges with that a part of water without sand-bed filter, then enters on-line detecting system; The backwash water of sand-bed filter enters intermediate water reuse system through the 8th valve.
It is simple in structure, stable, with low cost that the present invention has, and reduces quantity of wastewater effluent and advantage free from environmental pollution.
The accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Embodiment
As shown in Figure 1, the water outlet that the present invention includes synthetic ammonia circulating water system 1, described synthetic ammonia circulating water system 1 by pipeline with the first valve 3, the first water circulating pump 4, the second valve 5, water unit 2, the 3rd valve 6, the second water circulating pump 7, the 4th valve 8, with the 5th valve 9, be connected successively, described the 5th valve 9 is connected with the water-in of synthetic ammonia circulating water system 1 by pipeline, is respectively arranged with water water supplement port and additional soft wa ter mouth on described synthetic ammonia circulating water system 1; A described water water supplement port is connected with a water tank 21 with 17, water ga(u)ges 19 of a water self-regulated valve successively by pipeline, described additional soft wa ter mouth pass through pipeline successively with soft water self-regulated valve 16, soft water under meter 18 is connected with soft water water tank 20; Be provided with the first threeway 23 between described the second water circulating pump 7 and the 4th valve 8, one end of described threeway by pipeline successively with the 6th valve 10, sand-bed filter 13 is connected with the 7th valve 11, be provided with the second threeway 24 between described the 4th valve 8 and the 5th valve 9, described the 7th valve 11 is connected with an end of the second threeway 24 by pipeline; The blow-off line of described sand-bed filter 13 is connected with intermediate water reuse system 22 with the 8th valve 12 successively; Be provided with on-line monitoring system 14 between described the 5th valve 9 and synthetic ammonia circulating water system 1,14, water self-regulated valves 17 of described on-line monitoring system are connected with turn-key system 15 respectively with soft water self-regulated valve 16.
Method for supplementing water of the present invention, its step is as follows:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, turn-key system 15 calculates the cycles of concentration of recirculated water according to the data that transmit in step 1;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Embodiment mono-
The circulating water system internal circulating load is 6000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 3;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 0 ℃, and soft water is minimum is 36m
3/ h, one time the maximum consumptions of water are 54m
3/ h.
Embodiment bis-
The circulating water system internal circulating load is 6000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 5;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 40 ℃, and soft water is minimum is 85.4m
3/ h, one time the maximum consumptions of water are 33.6m
3/ h.
Embodiment tri-
The circulating water system internal circulating load is 6000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 4;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 40 ℃, and soft water is minimum is 76.8m
3/ h, one time the maximum consumptions of water are 51.2m
3/ h.
Embodiment tetra-
The circulating water system internal circulating load is 9000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 3;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 0 ℃, and soft water is minimum is 51m
3/ h, one time the maximum consumptions of water are 81m
3/ h.
Embodiment five
The circulating water system internal circulating load is 9000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 5;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 40 ℃, and soft water is minimum is 129.6m
3/ h, one time the maximum consumptions of water are 50.4m
3/ h.
Embodiment six
The circulating water system internal circulating load is 9000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 4;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 40 ℃, and soft water is minimum is 115.2m
3/ h, one time the maximum consumptions of water are 76.8m
3/ h.
Embodiment seven
The circulating water system internal circulating load is 12000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 3;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 0 ℃, and soft water is minimum is 72m
3/ h, one time the maximum consumptions of water are 108m
3/ h.
Embodiment eight
The circulating water system internal circulating load is 12000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 5;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 40 ℃, and soft water is minimum is 172.8m
3/ h, one time the maximum consumptions of water are 67.2m
3/ h.
Embodiment nine
The circulating water system internal circulating load is 12000m
3/ h:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system 1 by on-line monitoring system 14, and data are sent in turn-key system 15;
Two, the cycles of concentration that turn-key system 15 calculates recirculated water according to the data that transmit in step 1 is 4;
Three, the ratio that turn-key system 15 is controlled soft water self-regulated valve 16 and a water self-regulated valve 17 by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Temperature is 40 ℃, and soft water is minimum is 153.6m
3/ h, one time the maximum consumptions of water are 102.4m
3/ h.
Claims (2)
1. a synthetic ammonia circulating water system water replanishing device, comprise synthetic ammonia circulating water system (1), the water outlet of described synthetic ammonia circulating water system (1) by pipeline successively with the first valve (3), the first water circulating pump (4), the second valve (5), water unit (2), the 3rd valve (6), the second water circulating pump (7), the 4th valve (8) is connected with the 5th valve (9), described the 5th valve (9) is connected with the water-in of synthetic ammonia circulating water system (1) by pipeline, it is characterized in that: be respectively arranged with water water supplement port and additional soft wa ter mouth on described synthetic ammonia circulating water system (1), a described water water supplement port by pipeline successively with a water self-regulated valve (17), a water ga(u)ge (19) is connected with a water tank (21), described additional soft wa ter mouth by pipeline successively with soft water self-regulated valve (16), soft water under meter (18) is connected with soft water water tank (20), be provided with the first threeway (23) between described the second water circulating pump (7) and the 4th valve (8), one end of described threeway by pipeline successively with the 6th valve (10), sand-bed filter (13) is connected with the 7th valve (11), be provided with the second threeway (24) between described the 4th valve (8) and the 5th valve (9), described the 7th valve (11) is connected with an end of the second threeway (24) by pipeline, the blow-off line of described sand-bed filter (13) is connected with intermediate water reuse system (22) with the 8th valve (12) successively, be provided with on-line monitoring system (14) between described the 5th valve (9) and synthetic ammonia circulating water system (1), described on-line monitoring system (14), a water self-regulated valve (17) is connected with turn-key system (15) respectively with soft water self-regulated valve (16).
2. the method for supplementing water with synthetic ammonia circulating water system water replanishing device claimed in claim 1, it is characterized in that: its step is as follows:
One, detect circulating water quality and the water yield in synthetic ammonia circulating water system (1) by on-line monitoring system (14), and data are sent in turn-key system (15);
Two, turn-key system (15) calculates the cycles of concentration of recirculated water according to the data that transmit in step 1;
Three, the ratio that turn-key system (15) is controlled soft water self-regulated valve (16) and a water self-regulated valve (17) by the recirculated water cycles of concentration of gained in step 2 is carried out moisturizing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210058394.7A CN102583440B (en) | 2012-03-08 | 2012-03-08 | Water replenishing device of synthetic ammonia circulating water system and water replenishing method |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210058394.7A CN102583440B (en) | 2012-03-08 | 2012-03-08 | Water replenishing device of synthetic ammonia circulating water system and water replenishing method |
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| Publication Number | Publication Date |
|---|---|
| CN102583440A CN102583440A (en) | 2012-07-18 |
| CN102583440B true CN102583440B (en) | 2014-01-01 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210058394.7A Active CN102583440B (en) | 2012-03-08 | 2012-03-08 | Water replenishing device of synthetic ammonia circulating water system and water replenishing method |
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| CN (1) | CN102583440B (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1076713C (en) * | 1995-12-01 | 2001-12-26 | 徐保安 | Improved power plant water and ash treatment system |
| CN202643334U (en) * | 2012-03-08 | 2013-01-02 | 河南心连心化肥有限公司 | Water replenishing device of synthetic ammonia circulating water system |
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| CP03 | Change of name, title or address |
Address after: 453731 Xinxiang Economic Development Zone, Henan Province (Xiaoji Town) Patentee after: Henan Xinlianxin Chemical Industry Group Co., Ltd. Address before: 453731 Henan Xinxiang Economic Development Zone Xiaoji Town Henan Xinlianxin Chemical Fertilizer Co., Ltd. Patentee before: Henan XInlianxin Fertiliser Limited Company |
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| TR01 | Transfer of patent right |
Effective date of registration: 20200408 Address after: 453731 Xinxiang Economic Development Zone, Henan Province (Xiaoji Town) Co-patentee after: Jiujiang Xinlianxin Chemical Fertilizer Co.,Ltd. Patentee after: Henan Xinlianxin Chemical Industry Group Co.,Ltd. Co-patentee after: XINJIANG XINLIANXIN ENERGY CHEMICAL Co.,Ltd. Address before: 453731 Xinxiang Economic Development Zone, Henan Province (Xiaoji Town) Patentee before: Henan Xinlianxin Chemical Industry Group Co.,Ltd. |
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| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 453731 Xinxiang City, Henan Province Economic Development Zone (Xiaoji town) Patentee after: Henan Xinlianxin Chemical Industry Group Co.,Ltd. Patentee after: Jiangxi xinlianxin Chemical Industry Co.,Ltd. Patentee after: XINJIANG XINLIANXIN ENERGY CHEMICAL Co.,Ltd. Address before: 453731 Xinxiang City, Henan Province Economic Development Zone (Xiaoji town) Patentee before: Henan Xinlianxin Chemical Industry Group Co.,Ltd. Patentee before: Jiujiang Xinlianxin Chemical Fertilizer Co.,Ltd. Patentee before: XINJIANG XINLIANXIN ENERGY CHEMICAL Co.,Ltd. |