CN204026651U - A kind of closed condensate water recovery device - Google Patents
A kind of closed condensate water recovery device Download PDFInfo
- Publication number
- CN204026651U CN204026651U CN201420451300.7U CN201420451300U CN204026651U CN 204026651 U CN204026651 U CN 204026651U CN 201420451300 U CN201420451300 U CN 201420451300U CN 204026651 U CN204026651 U CN 204026651U
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- water
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- condensed water
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 206
- 238000011084 recovery Methods 0.000 title claims abstract description 29
- 238000004064 recycling Methods 0.000 claims abstract description 79
- 230000003020 moisturizing effect Effects 0.000 claims abstract description 18
- 239000013589 supplement Substances 0.000 claims abstract description 18
- 230000008676 import Effects 0.000 claims abstract description 11
- 239000010865 sewage Substances 0.000 claims abstract description 9
- 230000003068 static effect Effects 0.000 claims description 6
- 230000000694 effects Effects 0.000 abstract description 6
- 239000000126 substance Substances 0.000 abstract description 5
- 239000003054 catalyst Substances 0.000 abstract description 4
- 230000003628 erosive effect Effects 0.000 abstract description 4
- 238000012824 chemical production Methods 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000003911 water pollution Methods 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- 238000007701 flash-distillation Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
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- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
A kind of closed condensate water recovery device belongs to industrial condensed water recovery technology field, is specifically related to a kind of closed condensate water recovery device that coordinates chemical catalyst synthesizer.The utility model provides one to be applicable to chemical production field, is not subject to condensed water pollution effect, and there will not be the not closed condensate water recovery device of smooth situation of backwater.Of the present utility model being characterised in that: condensed water recycling can top is provided with water supplement port, the exit of described condensed water recycling can bottom is provided with filter, cool down erosion device and fast arranging device, and fast arranging device is connected with recycling can water pump; Recycling can water pump is connected with boiler by backwater control valve group; The water supplement port of described boiler and condensed water recycling can is all connected with moisturizing softening water tank by small pump; Between the water supplement port of described small pump and condensed water recycling can, be provided with moisturizing control valve group; The condensate water import department of described condensed water recycling can is provided with drain valve group; Described condensed water recycling can is provided with sewage draining exit corresponding to filter.
Description
Technical field
The utility model belongs to industrial condensed water recovery technology field, is specifically related to a kind of closed condensate water recovery device that coordinates chemical catalyst synthesizer.
Background technology
As everyone knows, in industrial production, steam, as a kind of purposes energy very widely, is used to realize industrial product process procedure.And steam discharges the condensed water generating after partial heat energy often by line.This is that the i.e. efficiency of heating surface just must discharge condensed water low heat transfer efficiency as early as possible from steam because will improve the production efficiency of steam use equipment, and clearly this is a kind of waste.
Present most enterprises or has done boiler steam condensate-water recovery operation, instead of goes out in line condensed water as before.Because boiler steam condensate-water reclaim be improve boiler operating efficiency significantly, effective method, and the economic interests that produce are also maximum.Not only the waste heat of discharge has obtained effective utilization, has also saved on the other hand the chemicals of water resource and water treatment.The condensation water recovery system of an obvious successful operation, to saving energy and reduce the cost, increase economic efficiency important effect.
The effect that condensed water reclaims is to recycle heat and the demineralized water of condensed water, can adopt different process mode according to different situations.In general custom, there is dividing of open system and closed system, just carry out simply to introduce these two kinds of methods that condensed water reclaims below.
Open system, this system condensing water collection tank is open type, communicates with atmosphere, and while entering collecting box due to condensed water, pressure reduces suddenly, and water temperature, higher than boiling point corresponding to this pressure, produces a large amount of secondary flash steams, and residue condensate temperature is approximately 100 DEG C.In fact,, due to flash distillation heat radiation or sometimes in order to prevent that transportation water pump cavitation is blended into cold water, reclaim water temperature only 70 DEG C of left and right.In addition Recovery with Open-loop mode has air and enters condensed water recovery channel, easily causes corrosive pipeline.But open system device is simple, invest less.Compared with directly discharging with condensed water, still have certain energy-saving effect.
Closed system, in this system, condensed water collecting box is closed, and in system, condensed water pressure remains higher than atmospheric pressure, and make condensed water water temperature lower than the boiling point under this pressure, the heat energy of condensed water is fully used.And the original quality of the condensed water of closed system maintenance steam, during for boiler feedwater, can not increase dissolved oxygen content, also reduce boiler replenishing water amount, reduce the expense of water treatment.
Existing enclosed condensation water recovery system, applied environment is comparatively simple conventionally, and conventionally can there is not contaminated situation in condensed water, and therefore, its recovery is also comparatively easy.But, some chemical fields (as catalyst synthetic etc.), chemicals need to move in multiple operations; And in moving process, can pollute condensed water; If these contaminated condensed waters directly enter in boiler, can cause boiler to break down, reduce boiler service life.
In addition, due to distant between catalyst-assembly and condensate water recovery device, pipeline is longer, cause dilatation pressure drop at condensed water in high temperature in by pipe network course of conveying, existing closed condensate recovery device is prone to the not smooth situation of backwater, therefore, it cannot be applied to the chemical production field that pipeline is grown.
The 3rd, the rate of recovery of traditional enclosed condensation water recovery system and recovery heat are also lower, need to further improve.
Summary of the invention
The utility model is exactly for the problems referred to above, provides one to be applicable to chemical production field, is not subject to condensed water pollution effect, and there will not be the not closed condensate water recovery device of smooth situation of backwater.
For realizing above-mentioned purpose of the present utility model, the utility model adopts following technical scheme, the utility model comprises condensed water recycling can, condensed water recycling can side is provided with condensate water import, condensed water recycling can top is provided with stable-pressure device, condensed water recycling can surface is provided with level transmitting sensor and temperature sensor, condensed water recycling can bottom is provided with outlet, it is characterized in that: condensed water recycling can top is provided with water supplement port, the exit of described condensed water recycling can bottom is provided with filter, cool down and lose device and fast arranging device, fast arranging device is connected with recycling can water pump, recycling can water pump is connected with boiler by backwater control valve group, the water supplement port of described boiler and condensed water recycling can is all connected with moisturizing softening water tank by small pump, between the water supplement port of described small pump and condensed water recycling can, be provided with moisturizing control valve group, the condensate water import department of described condensed water recycling can is provided with drain valve group, described condensed water recycling can is provided with sewage draining exit corresponding to filter.
As a kind of preferred version of the present utility model, described recycling can water pump is set to two.
As another kind of preferred version of the present utility model, described recycling can water pump, backwater control valve group, moisturizing control valve group, level transmitting sensor are all connected with electrical control cubicles with temperature sensor.
As the third preferred version of the present utility model, in described condensed water recycling can, be provided with water separator and static mixer corresponding to water supplement port and condensate water import.
The beneficial effects of the utility model: 1, the utility model passes through screen pack, suspension in contaminated condensed water can be filtered out, and carry out blowdown by sewage draining exit, when emit sewage limpid gradually after, while meeting boiler instructions for use, close sewage draining exit, and start recycling can water pump, condensed water is pumped in boiler and used; Therefore, the utility model is of value to the catalyst prod production field that adapts to condensed water vulnerable to pollution.
2, the utility model, by moisturizing softening water tank is connected with the water supplement port of condensed water recycling can, can be introduced to the water supplement port of condensed water recycling can the normal temperature demineralized water of certain pressure, enters in condensed water Huis closed cans by moisturizing control valve group; Avoid occurring that the not smooth problem of backwater occurs.
3, the utility model is set to two by recycling can water pump, can adopt the form of a preparation and a use; And can, according to the start-stop of the water level control recycling can water pump in condensed water recycling can, start a recycling can water pump when high water level, when low water level, recycling can water pump is stopped transport, and when superelevation water level, two recycling can water pumps start simultaneously, and condensed water recycling can is normally moved.
4, in the utility model condensed water recycling can, be provided with water separator and static mixer; Be convenient to the abundant mixing of normal temperature demineralized water and condensed water, be convenient to control water temperature in condensed water recycling can and keep constant.
5, the whole encloseds of high-temperature steam condensed water that the utility model produces catalyst-assembly reclaim, and realize condensed water and leak vapour and reclaim maximization, preferentially utilizing under the condition of condensed water, save to greatest extent demineralized water and the energy.
6, ensureing, under the normal manufacturing condition of user, condensate water is carried out to complete enclosed recovery, condensate water, leakage vapour and the whole recyclings of flash steam, time solidifying coolant-temperature gage of raising condensed water.
7, thoroughly eliminate the thermal pollution causing because discharging condensate water and flash distillation secondary vapour, whole condensation water recovery system is that complete airtight system eliminates safe hidden trouble, and realizes cleaner production.
8, the condensate water reclaiming can not polluted by airborne oxygen again, can directly utilize, and saves water treatment expense and boiler fired coal and takes.
9, there is not cavitation in condensate pump under the state of carrying condensed water in high temperature, condensate water can be sent into boiler recycling.
10, by electric cabinet is set, can realize equipment fully automatic operation, steadily, guard without people.
11, use the utility model than traditional many recovery of closed recovery device condensate water 5%～20%; All reclaim flash distillation secondary vapour and drain valve and normally leak vapour; The heats 50%～70% that reclaim more.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In accompanying drawing, 1 is catalyst-assembly, 2 is drain valve group, 3 is condensate water import, 4 is fast arranging device, 5 is filter, 6 is the erosion device of cooling down, 7 is recycling can water pump, 8 is static mixer, 9 is water separator, 10 is temperature sensor, 11 is condensed water recycling can, 12 is stable-pressure device, 13 is level transmitting sensor, 14 is water supplement port, 15 is moisturizing control valve group, 16 is boiler, 17 is small pump, 18 is moisturizing softening water tank, 19 is backwater control valve group, 20 is electrical control cubicles.
Detailed description of the invention
The utility model comprises condensed water recycling can 11, condensed water recycling can 11 sides are provided with condensate water import 3, condensed water recycling can 11 tops are provided with stable-pressure device 12, condensed water recycling can 11 surfaces are provided with level transmitting sensor 13 and temperature sensor 10, condensed water recycling can 11 bottoms are provided with outlet, it is characterized in that: condensed water recycling can 11 tops are provided with water supplement port 14, the exit of described condensed water recycling can 11 bottoms is provided with filter 5, cool down erosion device 6 and fast arranging device 4, and fast arranging device 4 is connected with recycling can water pump 7; Recycling can water pump 7 is connected with boiler 16 by backwater control valve group 19; The water supplement port 14 of described boiler 16 and condensed water recycling can 11 is all connected with moisturizing softening water tank 18 by small pump 17; Between described small pump 17 and the water supplement port 14 of condensed water recycling can 11, be provided with moisturizing control valve group 15; Condensate water import 3 places of described condensed water recycling can 11 are provided with drain valve group 2; Described condensed water recycling can 11 is provided with sewage draining exit corresponding to filter 5.
As a kind of preferred version of the present utility model, described recycling can water pump 7 is set to two.
As another kind of preferred version of the present utility model, described recycling can water pump 7, backwater control valve group 19, moisturizing control valve group 15, level transmitting sensor 13 are all connected with electrical control cubicles 20 with temperature sensor 10.
As the third preferred version of the present utility model, in described condensed water recycling can 11, be provided with water separator 9 and static mixer 8 corresponding to water supplement port 14 and condensate water import 3.
Described water separator 9 can be corrugated plate packing; The described erosion device 6 of cooling down can be screen waviness packings.
Below in conjunction with brief description of the drawings one-off process of the present utility model:
Near boiler rooms 16, the utility model is installed and is reclaimed the condensate water that catalyst-assembly 1 produces.Catalyst-assembly 1 equipment is after heat transmission equipment, and the condensed water in high temperature of generation is concentrated by drain valve group 2, merges to a condensate water pipe network, is recovered to condensed water recycling can of the present utility model 11 the insides and goes.
Because catalyst-assembly 1 pipeline is distant, cause dilatation step-down at condensed water in high temperature in by pipe network course of conveying, not smooth in order to prevent causing backwater, ensure that high-temperature steam condensate water can be recovered to condensed water recycling can 11 the insides smoothly, need to pass through the normal temperature demineralized water of the small pump 17 Fen Yin mono-3 kilograms of pressure in tunnel, get back to condensed water recycling can 11 the insides by moisturizing control valve group 15, high-temperature steam condensate water and normal temperature demineralized water are by being built in the static mixer 8 on condensed water recycling can 11, stable-pressure device 12, water separator 9, filter 5, temperature sensor 10, level transmitting sensing device, after the adjusting of the cavitation that disappears device and fast arranging device 4, make condensing water temperature be controlled at the following 90 DEG C of left and right of an atmospheric pressure, and ensure that reclaimer is in atmospheric pressure state, and be that enclosed recovery does not have the discharge of secondary vapour.Be mainly the signal that sends by temperature sensor 10 regulates moisturizing control valve group 15 aperture size to electrical control cubicles 20, control the temperature that flow keeps water, make the condensate water of output keep constant temperature, hydrophobic stable continuously by stable-pressure device 12 maintenance equipment.
Due in the time that catalyst-assembly 1 is driven or is stopped, condensate water is easily contaminated, be recovered to condensed water recycling can 11 the insides, after filter 5 filtration treatment, and open in time condensed water recycling can 11 sewage draining exit below sewage is discharged, the condensate water of by the time discharging reaches after boiler 16 moisturizing standards, could condensate water be transported to boiler 16 by startup recycling can water pump 7 and recycle.
By operation of the present utility model, make condensed water secondary vapour and all reclaim with hot equipment steam that steam trap leaks, and being fully utilized, both save demineralized water resource, save again heat energy, thereby reduced production run cost.
Be understandable that, above about specific descriptions of the present utility model, only for being described, the utility model is not limited to the described technical scheme of the utility model embodiment, those of ordinary skill in the art is to be understood that, still can modify or be equal to replacement the utility model, to reach identical technique effect; Use needs as long as meet, all within protection domain of the present utility model.
Claims (4)
1. a closed condensate water recovery device, comprise condensed water recycling can (11), condensed water recycling can (11) side is provided with condensate water import (3), condensed water recycling can (11) top is provided with stable-pressure device (12), condensed water recycling can (11) surface is provided with level transmitting sensor (13) and temperature sensor (10), condensed water recycling can (11) bottom is provided with outlet, it is characterized in that: condensed water recycling can (11) top is provided with water supplement port (14), the exit of described condensed water recycling can (11) bottom is provided with filter (5), cool down and lose device (6) and fast arranging device (4), fast arranging device (4) is connected with recycling can water pump (7), recycling can water pump (7) is connected by the same boiler of backwater control valve group (19) (16), the water supplement port (14) of described boiler (16) and condensed water recycling can (11) is all connected with moisturizing softening water tank (18) by small pump (17), between the water supplement port (14) of described small pump (17) and condensed water recycling can (11), be provided with moisturizing control valve group (15), the condensate water import (3) of described condensed water recycling can (11) locates to be provided with drain valve group (2), described condensed water recycling can (11) is provided with sewage draining exit corresponding to filter (5).
2. a kind of closed condensate water recovery device according to claim 1, is characterized in that: described recycling can water pump (7) is set to two.
3. a kind of closed condensate water recovery device according to claim 1, is characterized in that: described recycling can water pump (7), backwater control valve group (19), moisturizing control valve group (15), level transmitting sensor (13) and temperature sensor (10) all same electrical control cubicles (20) are connected.
4. a kind of closed condensate water recovery device according to claim 1, is characterized in that: in described condensed water recycling can (11), be provided with water separator (9) and static mixer (8) corresponding to water supplement port (14) and condensate water import (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420451300.7U CN204026651U (en) | 2014-08-12 | 2014-08-12 | A kind of closed condensate water recovery device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420451300.7U CN204026651U (en) | 2014-08-12 | 2014-08-12 | A kind of closed condensate water recovery device |
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| Publication Number | Publication Date |
|---|---|
| CN204026651U true CN204026651U (en) | 2014-12-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420451300.7U Expired - Lifetime CN204026651U (en) | 2014-08-12 | 2014-08-12 | A kind of closed condensate water recovery device |
Country Status (1)
| Country | Link |
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| CN (1) | CN204026651U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105782701A (en) * | 2014-12-26 | 2016-07-20 | 天津鼎电气成套设备有限公司 | Substation box condensation water recovery device |
| CN113883918A (en) * | 2021-10-21 | 2022-01-04 | 河南中烟工业有限责任公司 | Automatic condensate water recovery device |
| CN116817621A (en) * | 2023-08-28 | 2023-09-29 | 山东齐成石油化工有限公司 | Device for recovering condensate water and exhaust steam by flash evaporation of high-temperature condensate water |
-
2014
- 2014-08-12 CN CN201420451300.7U patent/CN204026651U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105782701A (en) * | 2014-12-26 | 2016-07-20 | 天津鼎电气成套设备有限公司 | Substation box condensation water recovery device |
| CN113883918A (en) * | 2021-10-21 | 2022-01-04 | 河南中烟工业有限责任公司 | Automatic condensate water recovery device |
| CN116817621A (en) * | 2023-08-28 | 2023-09-29 | 山东齐成石油化工有限公司 | Device for recovering condensate water and exhaust steam by flash evaporation of high-temperature condensate water |
| CN116817621B (en) * | 2023-08-28 | 2023-10-27 | 山东齐成石油化工有限公司 | Device for recovering condensate water and exhaust steam by flash evaporation of high-temperature condensate water |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |