CN205676151U - The feedwater of zinc roasting relieving haperacidity, circulation - Google Patents
The feedwater of zinc roasting relieving haperacidity, circulation Download PDFInfo
- Publication number
- CN205676151U CN205676151U CN201620557052.3U CN201620557052U CN205676151U CN 205676151 U CN205676151 U CN 205676151U CN 201620557052 U CN201620557052 U CN 201620557052U CN 205676151 U CN205676151 U CN 205676151U
- Authority
- CN
- China
- Prior art keywords
- water
- relieving haperacidity
- feedwater
- circulation
- roasting
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn - After Issue
Links
Landscapes
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses feedwater, the circulation of a kind of zinc roasting relieving haperacidity, the main pipeline of relieving haperacidity water circulating pump outlet connects pipeline and is connected by communicating pipe to roasting water cooling pond, water supply pump and heat-exchanger pump, SO2The cooling backwater pipeline of blower motor winding is connected with relieving haperacidity circulating water pool, and relieving haperacidity and firing cycles water system integration simultaneously use；It is connected with gas colling tower filler, Safety water seal filler respectively at diluted acid plate type heat exchanger circulating water pipeline outlet pipe laying；SO2Oil cooler newly installed in blower fan Lubricating-oil Station is connected with motor cooling feedwater piping by waterpipe, and circulating water pipeline and a waterpipe add communicating pipe, and oil cooler water return pipeline is connected with doing the suction circulating slot technique pipeline that adds water；Reach to save a water consumption by the feedwater of relieving haperacidity roasting, cleaning system, sulfur dioxide unit and dry desorption system, the transformation respectively of circulation, save the purpose of fund.
Description
Technical field the utility model relates to the transformation on economy of water cousumption technical field of roasting acid making system, is specifically related to a kind of zinc
The feedwater of roasting relieving haperacidity, circulation.
Background technology relieving haperacidity subsidiary factory belongs to and uses water rich and influential family, and by systematic influence and manufacturing technique requirent, every day requires supplementation with once
About 1200 tons of water, outer draining about 700 tons, it is mainly manifested in the following aspects: waft water loss for (1), cooling tower；(2), roast
Fire moisturizing and the draining of acid circulating pump room circulating water pool；(3), the moisturizing of cleaning system technique and draining (waste acid)；(4), do
Desorption system technique adds water；(5)、SO2The motor cooling water of blower fan.Before transformation, each moisturizing point of acid making system is raw by company
Produce water supply network and carry out moisturizing, and outer draining is exhausted directly to environmental protection workshop, does not recycle, and causes great lot of water resources
Waste.
Content of the invention the utility model provides the feedwater of a kind of zinc roasting relieving haperacidity, circulation, by relieving haperacidity roasting
Feedwater, circulation, the feedwater of cleaning system, circulation, the feedwater of sulfur dioxide unit, circulation, dry suction
The feedwater of system, the transformation respectively of circulation reach to save a water consumption, save the purpose of fund.
The technical scheme that the utility model provides to solve technical problem is as follows:
The feedwater of a kind of zinc roasting relieving haperacidity, circulation, including relieving haperacidity roasting feedwater, circulation, cleaning system
Feedwater, circulation, the feedwater of sulfur dioxide unit, circulation, the feedwater of dry desorption system, circulation；
Described relieving haperacidity roasting feedwater, the roasting relieving haperacidity circulating pump room of circulation include relieving haperacidity circulating water pool, relieving haperacidity
Water circulating pump, water cooling pond, hot-tub, water supply pump, heat-exchanger pump, cooling tower, connect on the main pipeline of relieving haperacidity water circulating pump outlet
Pipeline was connected to roasting water cooling pond, described water supply pump and heat-exchanger pump by communicating pipe, SO2Blower motor winding cool back water pipe
Road is connected with described relieving haperacidity circulating water pool, installs going out of welded tube branch and firing cycles water pump at relieving haperacidity water circulating pump outlet conduit
Mouth is connected, and installs welded tube at heat-exchanger pump outlet conduit and branches to relieving haperacidity circulating water pool, and the water collection device of described cooling tower is " M "
Type；
The feedwater of described cleaning system, circulation include diluted acid plate type heat exchanger, gas colling tower, Safety water seal,
At diluted acid plate type heat exchanger circulating water pipeline outlet pipe laying respectively with gas colling tower filler, Safety water seal filler even
Connect；
The feedwater of described sulfur dioxide unit, circulation include SO2Blower fan Lubricating-oil Station, SO2Blower fan Lubricating-oil Station increases by one
Platform oil cooler, is installed in series with crude cooler, and newly installed oil cooler is by a waterpipe and motor cooling feedwater
Pipeline connects, and a waterpipe is provided with valve, and circulating water pipeline and a waterpipe add communicating pipe；
The feedwater of described dry desorption system, circulation include SO2Blower fan Lubricating-oil Station, SO2Blower fan Lubricating-oil Station increases an oil
Cooler, oil cooler water return pipeline is connected with the dry circulating slot technique pipeline that adds water of inhaling.
The beneficial effects of the utility model: the 1st, the transformation of Sulfuric Acid Circulation Pump room cooling column water receiver, by statistical computation,
After changing high-efficient water-recovering device, the water loss about 130 tons that wafts can be reduced every day, water loss about 45000 tons can be reduced the whole year, by often
Water price lattice 2 yuan meter in Dun, can save fund more than 90,000 yuan every year；2nd, relieving haperacidity and firing cycles water system integration use by stopping every year
Water supply pump and 6 months meters of roasting cooling tower, every year can power cost saving 18.2 ten thousand yuan；Waft average every day water loss by roasting cooling tower
20 tons of meters, can save water rate 1.8 ten thousand yuan every year；Two add up to annual saving expense 200,000 yuan；3rd, the transformation on economy of water cousumption of cleaning system
Purify based on subsider discharge waste acid and Safety water seal moisturizing total 400 tons by every day, 400 tons of water can be saved every day, reclaim
Utilize 400 tons of outer drainings, add up to and annual save 132000 tons of water, reclaims 132000 tons of outer drainings, press per ton at present once
5 yuan of water meter, can save fund about 660,000 yuan every year；4th, every day is saved 80 tons of water in the transformation on economy of water cousumption of dry desorption system, adds up to
26400 tons of annual water of saving, based on 5 yuan of a water per ton at present, can save nearly fund 13.2 ten thousand yuan, to sum up institute every year
State, the transformation on economy of water cousumption of roasting acid making system, about 220,000 tons of annual water of saving, reclaim and reduce discharging about 270,000 tons, every year may be used
Saving fund 1,080,000 yuan.
Brief description Fig. 1 is the feedwater of sulfuric acid pump house, circulation plane before transformation；
Fig. 2 is the feedwater of sulfuric acid pump house, circulation plane after transformation；
Fig. 3 is sulfuric acid pump house firing cycles water system plane before transformation；
Fig. 4 is sulfuric acid pump house relieving haperacidity circulation plane before transformation；
Fig. 5 is sulfuric acid pump house circulation plane after transformation；
Fig. 6 is cleaning system feedwater, recirculated water plane before transformation；
Fig. 7 is transformation after-purification system feedwater, recirculated water plane；
Fig. 8 is sulfur dioxide unit recirculated water, feedwater piping plane before transformation；
Fig. 9 is sulfur dioxide unit recirculated water, feedwater piping plane after transformation；
Figure 10 is the feedwater of dry desorption system, recirculated water plane.
The feedwater of detailed description of the invention a kind of zinc roasting relieving haperacidity, circulation, including relieving haperacidity roasting feedwater, recirculated water
System, the feedwater of cleaning system, circulation, the feedwater of sulfur dioxide unit, circulation, the feedwater of dry desorption system,
Circulation；
The remodeling method of roasting relieving haperacidity circulating pump room: connect a DN50mm pipeline on relieving haperacidity circulating-pump outlet main pipeline
To roasting water cooling pond, it is achieved the moisturizing to roasting pond, use Valve controlling rate of water make-up；Install one at water supply pump and heat-exchanger pump to connect
Pipe, in order to regulate the liquid level in hot and cold pond, overflows after preventing hot water water full；SO2The cooling water of blower motor winding is by producing
The water that water supply network provides cools down, and its cooling backwater pipeline is connected with relieving haperacidity circulating water pool, it is achieved circulate relieving haperacidity
The moisturizing in pond, the moisturizing of such circulating water pool no longer with intrinsic production feedwater piping, has only been cleared up at parking maintenance
When needing behind pond toward pond water filling, just use this pipeline.The feedwater of improved sulfuric acid pump house, circulation are as shown in Figure 2.
Relieving haperacidity and firing cycles water system integration simultaneously use: roasting relieving haperacidity circulating pump room relieving haperacidity circulation and roasting follow
Ring water system is two each independent cover systems.Roasting relieving haperacidity circulating pump room relieving haperacidity circulation and firing cycles water system
Remodeling method: at relieving haperacidity water circulating pump outlet conduit, Φ 273 × 6 welded tube branch is installed and is connected with firing cycles water delivery side of pump
Connect, Φ 250 butterfly valve and flowmeter control water yield size are installed；At heat-exchanger pump outlet conduit, Φ 273 × 6 welded tube is installed and branches to system
Acid circulating water pool, makes the cooling backwater of inflow hot-tub without cooling tower, is pumped directly into relieving haperacidity circulating water pool, as shown in Figure 5.When
When outdoor temperature is less than 10 degree, it is possible to stop water supply pump and roasting cooling tower electric machine, open and close control valve, by relieving haperacidity recirculated water
Pump directly feeds roasting system cooling water, thus reaches the purpose of water-saving and electricity-saving.When environment temperature is higher than 10 degree, open and close control
Valve, enables original system and supplies water.When roasting cooling tower have an accident short-term be difficult to recover when, enable this covering device, it is ensured that roasting
Recirculated cooling water regular supply, is unlikely to impact and produces.
The transformation of Sulfuric Acid Circulation Pump room cooling column water receiver: originally used old-fashioned " V " type water collection device, water rate mistake of wafing
High.Remodeling method will use " V " type water collection device at present, is replaced by " M " type high-efficient water-recovering device." M " heavy duty detergent assembly type is received
Hydrophone, material is PVC, has the flame-retarding characteristic of resistance to combustion self-extinguishment；Planform is frame-type, receives water effect good；Meanwhile, this receipts water
Device piece intensity is high, indeformable, easy to maintenance.
The moisturizing of described cleaning system, the transformation of drainage system: install in the outlet of diluted acid plate type heat exchanger circulating water pipeline
A piece DN100mm pipeline is connected with gas colling tower filler, installs a DN50mm pipeline and Safety water seal filler simultaneously
Connect, make the moisturizing of gas colling tower and Safety water seal be produced, by original, the outer draining that feedwater changes recirculated water into, when purifying system
System discharges waste acid to environmental protection workshop, when the reduction of gas colling tower recycle acid liquid level needs to add water, and the moisturizing in tower with this pipeline, from
And make the outer draining of relieving haperacidity circulation be recycled utilization.So can save about 400 tons of water every day.Improved
Polished feedwater, circulation are as shown in Figure 7.
The transformation on economy of water cousumption of sulfur dioxide unit: in order to solve the higher problem of bearing bush temperature, save a water, take following
Measure: being further added by an oil cooler, former cooler is installed in series with oil, lubricating oil passes sequentially through two coolers and carries out cold
But；In order to improve cooling effect, newly installed cooler uses a water, and water source is taken in peace one on motor cooling feedwater piping
Root DN50mm arm, uses the Valve controlling water yield, and the backwater of cooler is connected to dry circulating slot technique of inhaling and adds water pipeline, as dry suction
The technique moisturizing of regulation recycle acid concentration, reaches to save the purpose of a water；Circulating water pipeline and a waterpipe add communicating pipe,
Switch over control with valve, it is achieved circulating water temperature relatively water supplement heat rejecter of Gao Shitong, and when one party breaks down
Complementation can be carried out when cutting off the water supply.Improved recirculated water, water supply system are as shown in Figure 9.
Dry desorption system transformation on economy of water cousumption: dry desorption system needs to add water to regulate recycle acid concentration, and water is used averagely once a day
The water yield about 80 tons, dry suction adds water all the time by grid supply of plant area.SO after transformation2Blower fan Lubricating-oil Station adds one
Oil cooler, oil cooler water return pipeline is connected with the dry technique pipeline that adds water of inhaling, adds water as dry technique of inhaling with cooler backwater,
No longer add water from a grid, thus saved a water consumption.The feedwater of improved dry desorption system, recirculated water plane are such as
Shown in Figure 10.
Claims (5)
1. the feedwater of zinc roasting relieving haperacidity, a circulation, including relieving haperacidity roasting feedwater, circulation, cleaning system
Feedwater, circulation, the feedwater of sulfur dioxide unit, circulation, the feedwater of dry desorption system, circulation, it is special
Levy and be: described relieving haperacidity roasting feedwater, the roasting relieving haperacidity circulating pump room of circulation include that relieving haperacidity circulating water pool, relieving haperacidity follow
Ring water pump, water cooling pond, hot-tub, water supply pump, heat-exchanger pump, cooling tower, connecting tube on the main pipeline of relieving haperacidity water circulating pump outlet
Road was connected to roasting water cooling pond, described water supply pump and heat-exchanger pump by communicating pipe, SO2The cooling backwater pipeline of blower motor winding
It is connected with described relieving haperacidity circulating water pool, at relieving haperacidity water circulating pump outlet conduit, welded tube branch and firing cycles water delivery side of pump are installed
Being connected, installing welded tube at heat-exchanger pump outlet conduit and branch to relieving haperacidity circulating water pool, the water collection device of described cooling tower is " M " type；
The feedwater of described cleaning system, circulation include diluted acid plate type heat exchanger, gas colling tower, Safety water seal, dilute
Acid plate type heat exchanger circulating water pipeline outlet pipe laying is connected with gas colling tower filler, Safety water seal filler respectively；
The feedwater of described sulfur dioxide unit, circulation include SO2Blower fan Lubricating-oil Station, SO2Blower fan Lubricating-oil Station increases an oil
Cooler, is installed in series with crude cooler, and newly installed oil cooler cools down feedwater piping by a waterpipe with motor
Connecting, a waterpipe is provided with valve, and circulating water pipeline and a waterpipe add communicating pipe；
The feedwater of described dry desorption system, circulation include SO2Blower fan Lubricating-oil Station, SO2Blower fan Lubricating-oil Station increases an oil cooling but
Device, oil cooler water return pipeline is connected with the dry circulating slot technique pipeline that adds water of inhaling.
2. the feedwater of a kind of zinc roasting relieving haperacidity according to claim 1, circulation, it is characterised in that: described relieving haperacidity
Roasting feedwater, circulation roasting relieving haperacidity circulating pump room relieving haperacidity circulating-pump outlet main pipeline on meet a DN50mm
Pipeline is to roasting water cooling pond.
3. the feedwater of a kind of zinc roasting relieving haperacidity according to claim 1, circulation, it is characterised in that: described relieving haperacidity
Roasting feedwater, relieving haperacidity circulating-pump outlet Pipe installing Φ 273 × 6 welded tube of roasting relieving haperacidity circulating pump room of circulation divide
Prop up and be connected with firing cycles water delivery side of pump, Φ 250 butterfly valve and flowmeter are installed.
4. the feedwater of a kind of zinc roasting relieving haperacidity according to claim 1, circulation, it is characterised in that: described relieving haperacidity
Roasting feedwater, circulation roasting relieving haperacidity circulating pump room heat-exchanger pump outlet conduit install Φ 273 × 6 welded tube branch to
Relieving haperacidity circulating water pool.
5. the feedwater of a kind of zinc roasting relieving haperacidity according to claim 1, circulation, it is characterised in that: described purification
A DN100mm pipeline and gas are installed in the feedwater of system, the diluted acid plate type heat exchanger circulating water pipeline outlet of circulation
Cooling tower filler connects, and installs a DN50mm pipeline simultaneously and is connected with Safety water seal filler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620557052.3U CN205676151U (en) | 2016-06-08 | 2016-06-08 | The feedwater of zinc roasting relieving haperacidity, circulation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620557052.3U CN205676151U (en) | 2016-06-08 | 2016-06-08 | The feedwater of zinc roasting relieving haperacidity, circulation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205676151U true CN205676151U (en) | 2016-11-09 |
Family
ID=57435552
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620557052.3U Withdrawn - After Issue CN205676151U (en) | 2016-06-08 | 2016-06-08 | The feedwater of zinc roasting relieving haperacidity, circulation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205676151U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106395762A (en) * | 2016-06-08 | 2017-02-15 | 赤峰中色锌业有限公司 | Water supply and circulating water systems applied to roasting of zinc for acid making |
-
2016
- 2016-06-08 CN CN201620557052.3U patent/CN205676151U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106395762A (en) * | 2016-06-08 | 2017-02-15 | 赤峰中色锌业有限公司 | Water supply and circulating water systems applied to roasting of zinc for acid making |
| CN106395762B (en) * | 2016-06-08 | 2018-03-30 | 赤峰中色锌业有限公司 | The feedwater of zinc roasting relieving haperacidity, circulation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203687003U (en) | Boiler regular blowdown drainage recovery system | |
| CN104019580B (en) | A kind of low wind-warm syndrome operating mode mine return air source heat pump system and the method for operation thereof | |
| CN103604244A (en) | Multi-resource low-temperature waste heat comprehensive utilization system | |
| CN201241706Y (en) | Waste water cycling and reutilizing apparatus of open type tunnel boring machine | |
| CN204574340U (en) | Subterranean heat exchanger of earth source heat pump water collecting and diversifying device system | |
| CN103984999B (en) | A kind of industrial circulating cooling water energy integrated optimization method | |
| CN108194052A (en) | A kind of mine water residual heat direct heating system | |
| CN207728346U (en) | A kind of mine water residual heat direct heating system | |
| CN111238132B (en) | Energy-saving industrial circulating water system and operation method thereof | |
| CN205676151U (en) | The feedwater of zinc roasting relieving haperacidity, circulation | |
| CN107421163A (en) | Air electric energy twin-stage heating and refrigerating system and heating and refrigerating method | |
| CN208253697U (en) | A kind of geothermal heating operating system of accumulation of heat and multistage terminal user's combined heat | |
| CN107327311B (en) | A kind of long tunnel gas source cooling system | |
| CN106395762B (en) | The feedwater of zinc roasting relieving haperacidity, circulation | |
| CN205156210U (en) | Take auxiliary cold source's ocean refrigerated water concentrated cooling system | |
| CN204677440U (en) | The pre-heat recovery system of a kind of screw air compressor | |
| CN211373282U (en) | Steam condensate gas recovery device | |
| CN104100314B (en) | A kind of condensed steam type small steam turbine exhaust steam bootstrap system driving induced draught fan | |
| CN208936369U (en) | A kind of self-circulating energy-saving type water cooling air conditioning system | |
| CN203785523U (en) | Tower charging pipeline flow combination and distribution structure for cooling towers with external water turbines | |
| CN105240970A (en) | Sea-chilled-water concentrated cold supplying system with auxiliary cold source and concentrated cold supplying method | |
| CN205317014U (en) | No power cycle cooling tower | |
| CN206247697U (en) | A kind of centrifugal air compressor waste heat recycling system | |
| CN205580075U (en) | Cooling water circulation equipment of recycling | |
| CN205481481U (en) | Super large difference in temperature single tube long range transport water cold -storage cooling system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20161109 Effective date of abandoning: 20180330 |