CN206858217U - Mineral hot furnace is produced with softened water and recovery system - Google Patents
Mineral hot furnace is produced with softened water and recovery system Download PDFInfo
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- CN206858217U CN206858217U CN201720734160.8U CN201720734160U CN206858217U CN 206858217 U CN206858217 U CN 206858217U CN 201720734160 U CN201720734160 U CN 201720734160U CN 206858217 U CN206858217 U CN 206858217U
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Abstract
A kind of mineral hot furnace is produced with softened water and recovery system,Including saline device,Ion interchange unit,Tank,Saline device includes make-up tank,Delivery pump,Upper hose,Water level control meter,The internal cavities of cell body are divided into first inner chamber by the first partition and second partition of the make-up tank,Second inner chamber,3rd inner chamber,In the bottom of second inner chamber, second step is set,In the bottom of the 3rd inner chamber, the 3rd step is set,The input port of delivery pump connects brine outlet by input channel,The delivery outlet of delivery pump connects the input port of ion interchange unit by output channel,Upper hose is arranged on the top of the first inner chamber of make-up tank,In the utility model,Mixed impurity is deposited in the bottom land of first inner chamber first when preparing salt solution,Also can sediment fraction impurity in the bottom land of second inner chamber,Bottom land in the 3rd inner chamber can also depositing contaminants,This ensure that impurity or precipitation are not contained in the salt solution being extracted by conveying.
Description
Technical field
It the utility model is related to mineral hot furnace technology on circulating cooling water treatment field, more particularly to a kind of mineral hot furnace softened water
Production and recovery system.
Background technology
During mineral hot furnace use, heat is very high, and in order to cool to mineral hot furnace, generally use recirculated water drops for mineral hot furnace
Temperature, still, industrial running water mineral content are higher, fouling are easy to after being used for multiple times, and exchange heat for mineral hot furnace
After cooling, mineral matter in recirculated water because be heated separate out, the speed of fouling faster, hold very much containing more incrustation scale in recirculated water
Easily circulating water pipeline is blocked, this not only brings larger trouble to cleaning pipeline, and is made because of cleaning circulating water pipeline
It can not be cooled into mineral hot furnace, this brings great disadvantage to production, directly affects the normal production of mineral hot furnace or reduces
Production efficiency.
Generally, soft water is produced using ion-exchange, to go to remove water the content of mineral, so as to reduce the hair of fouling
It is raw, use the calcium ion in sodium ion and water in salt solution or magnesium ion to swap in ion-exchange, so firstly the need of
Salt solution is configured, salt and water are exactly added to dissolving in trough using the method for saline and form salt solution by most enterprises, but
It is, because industrial salt impurity, levels of precipitate are more, during salt dissolves, impurity and to be deposited in cell body
Bottom, when salt solution is discharged along brine outlet, partial impurities and precipitation can be conveyed with salt solution and be pumped into ion exchange dress
In putting, this not only causes very big infringement to ion interchange unit, can also influence the quality of soft water prepared.
The content of the invention
It is necessary to propose a kind of mineral hot furnace softened water production and recovery system for carrying out precipitating separation to salt impurities in water.
A kind of mineral hot furnace is produced with softened water and recovery system, including saline device, ion interchange unit, water storage
Pond, saline device are connected with ion interchange unit, and the salt solution prepared is sent into ion interchange unit, ion exchange dress
Put and be connected with tank, the soft water of generation is discharged into tank, tank sets delivery port, with being cooled down for mineral hot furnace
The water inlet connection of circulating water pipeline, saline device includes make-up tank, delivery pump, upper hose, water level control meter, described to match somebody with somebody
Groove processed is open-topped cell body, and first partition and second partition are set in the inside of cell body, by the internal cavities of cell body point
First inner chamber, second inner chamber, the 3rd inner chamber are segmented into, the top of first partition is concordant with the top of cell body, the bottom of first partition
It is not connected with the bottom of cell body, to form the salt solution communicating passage of first inner chamber and second inner chamber, the top of second partition and groove
The top of body is concordant, and the bottom of second partition is not connected with the bottom of cell body, to form the salt solution of second inner chamber and the 3rd inner chamber
Communicating passage, and the height of second partition is less than the height of first partition, second step is set in the bottom of second inner chamber, with shape
Into the bottom land of second inner chamber, the 3rd step is set in the bottom of the 3rd inner chamber, to form the bottom land of the 3rd inner chamber, first inner chamber
The height of bottom land, the height of the bottom land of second inner chamber, the height of bottom land of the 3rd inner chamber increase successively, the side wall in the 3rd inner chamber
On open up brine outlet, for the height of brine outlet higher than the height of the bottom land of the 3rd inner chamber, the input port of delivery pump passes through input
Pipeline connects brine outlet, and the delivery outlet of delivery pump connects the input port of ion interchange unit by output channel, and upper hose is set
Put in the top of the first inner chamber of make-up tank, water level control meter is arranged on upper hose, for detecting the salt solution water in make-up tank
Position, and be turned on and off according to testing result control upper hose.
Preferably, the bottom land of second inner chamber is tipper bottom, and the incline direction of the bottom land of second inner chamber is from close to the 3rd
The one of one laterally closer first inner chamber of inner chamber is sloped downwardly, and the bottom land of the 3rd inner chamber is tipper bottom, the groove of the 3rd inner chamber
The incline direction at bottom is consistent with the incline direction of the bottom land of second inner chamber.
Preferably, make-up tank includes outer wall, inwall and surrounds the heat insulation cavity formed by outer wall and inwall, empty in insulation
Intracavitary is passed through circulating hot water, thinks the water insulation in make-up tank, accelerates the speed that block salt is dissolved in water.
Preferably, make-up tank also sets up an overflow pipe, and the lower end of overflow pipe connects with the input port of delivery pump, overflows
The upper end in flow tube road is arranged on the top of the 3rd inner chamber.
Preferably, the mineral hot furnace is produced with softened water and recovery system also includes cooling device, and cooling device includes cold
But tower, return pipe, soft water outlet pipe, the distal end of return pipe are used to connect with the delivery port of the circulating water pipeline of mineral hot furnace cooling,
Cooling tower is delivered to the circulation soft water after being exchanged heat with mineral hot furnace, the near-end of return pipe extends to from the bottom up of cooling tower
The top of cooling tower, fan and some jet pipes being also set up at the top of cooling tower, some jet pipes connect with the near-end of return pipe, with
Soft water to be cooled is trickled down downwards along jet pipe, some natural wind entrances are also opened up in the side wall of cooling tower, so that by wind
Fan the natural wind sucked from bottom to top and the soft water fallen from the top down forms convection current, to cool to soft water, after cooling
Soft water falls to be connected in cooling tower bottom, one end of soft water outlet pipe with the bottom of cooling tower, the other end of soft water outlet pipe and storage
Pond is connected, and the soft water after cooling is delivered into tank.
Preferably, cooling device is also in charge of including water outlet, and one end that the water outlet is in charge of connects with soft water outlet pipe, water outlet
The other end being in charge of connects with the heat insulation cavity of make-up tank, to be incubated using the soft water after cooling down as make-up tank.
Preferably, the mineral hot furnace is produced with softened water and recovery system also includes well, water cooling pipe network, water cooling pipe network bag
Include be sequentially connected enter water tubule, spiral tubule, water outlet tubule, underground water is extracted out and delivered into water tubule, spiral tubule by well
It is that the taper pipe network formed is coiled by a tubule from the top down, the area that the tubule of lower floor is circular is circular more than upper strata tubule
Area, the water cooling pipe network are seated in the inside of cooling tower, and water cooling pipe network is arranged on jet pipe at the top of cooling tower and cooling tower
Between bottom, so that the soft water to be fallen from jet pipe is online in water cooling tube by sprinkle, water outlet tubule discharges the underground water after heat exchange.
Preferably, the water cooling pipe network also includes upper moisture pipe, and one end of upper moisture pipe connects with water outlet tubule, upper moisture
The other end of pipe is connected with the upper hose of make-up tank, and the underground water after heat exchange is delivered in make-up tank, for salt manufacturing
Water.
In the utility model, salt and water are first added into first inner chamber, preparation forms salt solution, and mixed impurity is heavy first
Form sediment in the bottom land of first inner chamber, lysigenous salt solution enters second inner chamber, second inner chamber bottom land also can sediment fraction it is miscellaneous
Matter, then salt solution enter the 3rd inner chamber, the 3rd inner chamber bottom land can also depositing contaminants, and by brine outlet set position
Higher than the bottom land height of the 3rd inner chamber, this ensure that not containing impurity or precipitation in the salt solution being extracted by conveying.
Brief description of the drawings
Fig. 1 is the structural representation of the production of mineral hot furnace softened water and recovery system.
Fig. 2 is the top view of the production of mineral hot furnace softened water and recovery system.
Fig. 3 is the upward view of the production of mineral hot furnace softened water and recovery system.
Fig. 4 is the front view of the saline device.
Fig. 5 is the top view of the saline device.
Fig. 6 is sectional views of the Fig. 5 along A-A.
Fig. 7 is the structural representation of the water cooling pipe network.
In figure：Saline device 10, make-up tank 11, first partition 111, second partition 112, first inner chamber 113, second
Inner chamber 114, the 3rd inner chamber 115, brine outlet 1151, second step 116, the 3rd step 117, heat insulation cavity 118, delivery pump
12nd, input channel 121, output channel 122, overflow pipe 123, upper hose 13, water level control meter 14, ion interchange unit 20,
Tank 30, delivery port 31, cooling device 40, cooling tower 41, fan 411, jet pipe 412, natural wind entrance 413, return pipe 42,
Soft water outlet pipe 43, water outlet are in charge of 44, water cooling pipe network 50, enter water tubule 51, spiral tubule 52, water outlet tubule 53, upper moisture pipe
54。
Embodiment
, below will be to required use in embodiment in order to illustrate more clearly of the technical scheme of the utility model embodiment
Accompanying drawing be briefly described, it should be apparent that, drawings in the following description are some embodiments of the utility model, for this
For the those of ordinary skill of field, on the premise of not paying creative work, it can also be obtained according to these accompanying drawings other
Accompanying drawing.
Referring to Fig. 1 to Fig. 6, the utility model embodiment provides a kind of mineral hot furnace softened water production and recovery system,
Including saline device 10, ion interchange unit 20, tank 30, saline device 10 connects with ion interchange unit 20
Connect, the salt solution prepared is sent into ion interchange unit 20, ion interchange unit 20 is connected with tank 30, by generation
Soft water is discharged into tank 30, and tank 30 sets delivery port 31, with the water inlet with the circulating water pipeline cooled down for mineral hot furnace
Connection.
Saline device 10 includes make-up tank 11, delivery pump 12, upper hose 13, water level control meter 14, and make-up tank 11 is
Open-topped cell body, first partition 111 and second partition 112 are set in the inside of cell body, by the internal cavities of cell body point
First inner chamber 113, second inner chamber 114, the 3rd inner chamber 115 are segmented into, the top of first partition 111 is concordant with the top of cell body, the
The bottom of one dividing plate 111 is not connected with the bottom of cell body, is led to forming first inner chamber 113 with the salt solution of second inner chamber 114 and connecting
Road, the top of second partition 112 is concordant with the top of cell body, and the bottom of second partition 112 is not connected with the bottom of cell body, with shape
Into the salt solution communicating passage of the inner chamber 115 of second inner chamber 114 and the 3rd, and the height of second partition 112 is less than first partition 111
Highly, second step 116 is set in the bottom of second inner chamber 114, to form the bottom land of second inner chamber 114, in the 3rd inner chamber 115
Bottom the 3rd step 117 is set, to form the bottom land of the 3rd inner chamber 115, the height of the bottom land of first inner chamber 113, in second
The height of the bottom land of chamber 114, the height of bottom land of the 3rd inner chamber 115 increase successively, and salt is opened up in the side wall of the 3rd inner chamber 115
Water out 1151, higher than the height of the bottom land of the 3rd inner chamber 115, the input port of delivery pump 12 passes through the height of brine outlet 1151
Input channel 121 connects brine outlet 1151, and the delivery outlet of delivery pump 12 connects ion interchange unit 20 by output channel 122
Input port, upper hose 13 is arranged on the top of the first inner chamber 113 of make-up tank 11, and water level control meter 14 is arranged on upper hose 13
On, it is turned on and off for detecting the saline water level in make-up tank 11, and according to testing result control upper hose 13.
Wherein, ion interchange unit 20 includes ion exchanger and water tank, the soft water that ion exchanger will be formed after exchange
It is discharged into water tank, the soft water in water tank enters tank 30 again.
Referring to Fig. 6, further, the bottom land of second inner chamber 114 is tipper bottom, the inclination side of the bottom land of second inner chamber 114
Xiang Weicong is sloped downwardly close to the one of a laterally closer first inner chamber 113 of the 3rd inner chamber 115, the bottom land of the 3rd inner chamber 115
It is consistent with the incline direction of the bottom land of second inner chamber 114 for tipper bottom, the incline direction of the bottom land of the 3rd inner chamber 115.Deposition
It can be moved in the impurity of bottom land along inclined bottom land to the bottom land of first inner chamber 113, so force impurity or precipitation away from salt
Water out 1151, free from admixture in salt solution is further ensured, and impurity is concentrated on to the bottom land of first inner chamber 113, be easy to clear
Reason.
Further, make-up tank 11 includes outer wall, inwall and the heat insulation cavity 118 formed is surrounded by outer wall and inwall, is protecting
Circulating hot water is passed through in warm cavity 118, the water insulation in make-up tank 11 is thought, accelerates the speed that block salt is dissolved in water.If
Warm water or hot water are added directly into make-up tank 11 to dissolve salt, the mineral matter in such water is easy to heated fouling, this skill
In art scheme, by the make-up tank 11 of chuck, heating is slowly stablized to the water in trough, avoids fouling.
Further, make-up tank 11 also sets up an overflow pipe 123, and the lower end of overflow pipe 123 is defeated with delivery pump 12
Entrance connects, and the upper end of overflow pipe 123 is arranged on the top of the 3rd inner chamber 115.When hydraulic pressure is excessive in delivery pump 12, hold very much
It is larger when hydraulic pressure is excessive in delivery pump 12 there is provided overflow pipe 123 in order to solve the problem easily by the scaling loss of delivery pump 12
Hydraulic pressure released by overflow pipe 123, into the 3rd inner chamber 115, to protect delivery pump 12.
Referring to Fig. 1 to Fig. 3, further, mineral hot furnace is produced with softened water and recovery system also includes cooling device 40, cools down
Device 40 includes cooling tower 41, return pipe 42, soft water outlet pipe 43, and the distal end of return pipe 42 is used for the circulation with mineral hot furnace cooling
The delivery port connection of waterpipe, the circulation soft water after being exchanged heat with mineral hot furnace are delivered to cooling tower 41, the near-end of return pipe 42
From the bottom up top for extending to cooling tower 41 of cooling tower 41, fan 411 and some is also set up at the top of cooling tower 41
Jet pipe 412, some jet pipes 412 connect with the near-end of return pipe 42, so that soft water to be cooled is trickled down downwards along jet pipe 412,
Some natural wind entrances 413 are also opened up in the side wall of cooling tower 41 so that the natural wind sucked from bottom to top by fan 411 with
The soft water fallen from the top down forms convection current, and to cool to soft water, the soft water after cooling falls in the bottom of cooling tower 41, soft water
One end of outlet pipe 43 connects with the bottom of cooling tower 41, and the other end of soft water outlet pipe 43 connects with tank 30, will be cold
But the soft water after is delivered to tank 30.
The temperature of circulation soft water after mineral hot furnace heat exchange is very high, but water quality is still soft water, can be recycled, so
Soft water is exchanged heat there is provided cooling device 40 and cooled, is reused for mineral hot furnace.
Further, cooling device 40 is also in charge of 44 including water outlet, and one end that water outlet is in charge of 44 connects with soft water outlet pipe 43,
Water outlet is in charge of 44 other end and connected with the heat insulation cavity 118 of make-up tank 11, to be protected using the soft water after cooling as make-up tank 11
Temperature.
The temperature of circulation soft water after mineral hot furnace heat exchange is up to 43 degree, and after the cooling of cooling tower 41, temperature is down to 37,38
Degree, and in order to avoid fouling in groove in make-up tank 11, the temperature of insulation can not be too high, so it is in charge of 44 there is provided water outlet,
On the premise of not changing pipeline layout, it is possible to play a part of being incubated make-up tank 11.
Referring to Fig. 1 to Fig. 3, and Fig. 7, further, mineral hot furnace is produced with softened water and recovery system also includes well, water cooling
Pipe network 50, what water cooling pipe network 50 included being sequentially connected enters water tubule 51, spiral tubule 52, water outlet tubule 53, and well is by underground water
Extraction is delivered into water tubule 51, and spiral tubule 52 is to coil the taper pipe network formed from the top down by a tubule, lower floor it is thin
Pipe ring around area be more than the circular area of upper strata tubule, water cooling pipe network 50 is seated in the inside of cooling tower 41, water cooling pipe network 50
It is arranged between the jet pipe 412 at the top of cooling tower 41 and the bottom of cooling tower 41, so that the soft water to fall from jet pipe 412 is by sprinkle
On water cooling pipe network 50, water outlet tubule 53 discharges the underground water after heat exchange.
As natural wind cooling supplement measure, because the underground water temperature released in well is very low, about 10 degree with
Under, exchanged heat using underground water and soft water, reduce further the temperature of soft water.
The tubule by underground water circulation is set to helicon pipe network simultaneously, and interior in the horizontal direction, spiral tubule 52 is most
The circular area of the tubule of bottom is about the 3/4 of the area of the bottom of cooling tower 41, successively upwards, in vertical direction, spiral
Tubule 52 has certain altitude, and height is about the 2/3 of the internal height of cooling tower 41, so that the inside of cooling tower 41 falls soft
Water is substantially all to be contacted with water cooling pipe network 50, realizes heat exchange cooling.
Further, water cooling pipe network 50 also includes upper moisture pipe 54, and one end of upper moisture pipe 54 connects with water outlet tubule 53, on
The other end of moisture pipe 54 is connected with the upper hose 13 of make-up tank 11, and the underground water after heat exchange is delivered into make-up tank 11
It is interior, for preparing salt solution.
Water used is also running water when being typically formulated salt solution, when the temperature of running water is low, it is necessary to individually heat, to add
The dissolution velocity of fast salt, this will increase a process or equipment to tap water heating insulation, and in the technical program, directly
Connect using the underground water after heat exchange to prepare salt solution, moderate temperature, and increase on the basis of original pipeline, without independent
The process or equipment of insulation are set, and cost is low, and effect is good.
Module or unit in the utility model embodiment device can be merged, divide and deleted according to being actually needed
Subtract.
Above disclosed is only the utility model preferred embodiment, can not limit the utility model with this certainly
Interest field, one of ordinary skill in the art will appreciate that realize all or part of flow of above-described embodiment, and according to this reality
The equivalent variations made with new claim, still fall within the scope that utility model is covered.
Claims (8)
1. a kind of mineral hot furnace is produced with softened water and recovery system, it is characterised in that：Filled including saline device, ion exchange
To put, tank, saline device is connected with ion interchange unit, and the salt solution prepared is sent into ion interchange unit, from
Sub- switch is connected with tank, and the soft water of generation is discharged into tank, and tank sets delivery port, with for ore deposit heat
The water inlet connection of the circulating water pipeline of stove cooling, saline device include make-up tank, delivery pump, upper hose, water level control
Meter, the make-up tank is open-topped cell body, first partition and second partition is set in the inside of cell body, by cell body
Portion's cavity is divided into first inner chamber, second inner chamber, the 3rd inner chamber, and the top of first partition is concordant with the top of cell body, first every
The bottom of plate is not connected with the bottom of cell body, to form the salt solution communicating passage of first inner chamber and second inner chamber, second partition
Top is concordant with the top of cell body, and the bottom of second partition is not connected with the bottom of cell body, to be formed in second inner chamber and the 3rd
The salt solution communicating passage of chamber, and the height of second partition is less than the height of first partition, and second is set in the bottom of second inner chamber
Step, to form the bottom land of second inner chamber, the 3rd step is set in the bottom of the 3rd inner chamber, to form the bottom land of the 3rd inner chamber,
The height of the bottom land of first inner chamber, the height of the bottom land of second inner chamber, the height of bottom land of the 3rd inner chamber increase successively, the 3rd
Brine outlet is opened up in the side wall of inner chamber, the height of brine outlet is higher than the height of the bottom land of the 3rd inner chamber, the input of delivery pump
Mouth connects brine outlet by input channel, and the delivery outlet of delivery pump passes through the input that output channel connects ion interchange unit
Mouthful, upper hose is arranged on the top of the first inner chamber of make-up tank, and water level control meter is arranged on upper hose, for detecting make-up tank
Interior saline water level, and be turned on and off according to testing result control upper hose.
2. mineral hot furnace as claimed in claim 1 is produced with softened water and recovery system, it is characterised in that：The bottom land of second inner chamber
For tipper bottom, the incline direction of the bottom land of second inner chamber is from the side of the laterally closer first inner chamber close to the 3rd inner chamber
Tilt down, the bottom land of the 3rd inner chamber is tipper bottom, the incline direction of the bottom land of the 3rd inner chamber and the bottom land of second inner chamber
Incline direction is consistent.
3. mineral hot furnace as claimed in claim 1 is produced with softened water and recovery system, it is characterised in that：Make-up tank includes outer
Wall, inwall and the heat insulation cavity formed is surrounded by outer wall and inwall, circulating hot water is passed through in heat insulation cavity, thinks make-up tank
Interior water insulation, accelerates the speed that block salt is dissolved in water.
4. mineral hot furnace as claimed in claim 1 is produced with softened water and recovery system, it is characterised in that：Make-up tank also sets up one
Root overflow pipe, the lower end of overflow pipe connect with the input port of delivery pump, and the upper end of overflow pipe is arranged on the 3rd inner chamber
Top.
5. mineral hot furnace as claimed in claim 3 is produced with softened water and recovery system, it is characterised in that：The mineral hot furnace is with soft
Changing aquatic production and recovery system also includes cooling device, and cooling device includes cooling tower, return pipe, soft water outlet pipe, return pipe
Distal end be used to connect with the delivery port of circulating water pipeline of mineral hot furnace cooling, the circulation soft water after being exchanged heat with mineral hot furnace is defeated
Deliver to cooling tower, the near-end of return pipe is from the bottom up top for extending to cooling tower of cooling tower, at the top of cooling tower also
Fan and some jet pipes, some jet pipes are set to be connected with the near-end of return pipe, so that soft water to be cooled is spilt downwards along jet pipe
Fall, some natural wind entrances also opened up in the side wall of cooling tower so that by the natural wind that fan sucks from bottom to top with from upper
The soft water fallen downwards forms convection current, and to cool to soft water, the soft water after cooling falls in cooling tower bottom, soft water outlet pipe
One end connected with the bottom of cooling tower, the other end of soft water outlet pipe connects with tank, by after cooling soft water convey
To tank.
6. mineral hot furnace as claimed in claim 5 is produced with softened water and recovery system, it is characterised in that：Cooling device also includes
Water outlet is in charge of, and one end that the water outlet is in charge of connects with soft water outlet pipe, and the insulation of the other end and make-up tank that water outlet is in charge of is empty
Chamber connects, to be incubated using the soft water after cooling down as make-up tank.
7. mineral hot furnace as claimed in claim 5 is produced with softened water and recovery system, it is characterised in that：The mineral hot furnace is with soft
Changing aquatic production and recovery system also includes well, water cooling pipe network, and it is thin that what water cooling pipe network included being sequentially connected enters water tubule, spiral
Underground water is extracted out and delivered into water tubule by pipe, water outlet tubule, well, and spiral tubule is to be coiled to be formed from the top down by a tubule
Taper pipe network, the circular area of the tubule of lower floor is more than the circular area of upper strata tubule, and the water cooling pipe network is seated in cooling
The inside of tower, water cooling pipe network are arranged between the jet pipe at the top of cooling tower and the bottom of cooling tower, so that it is soft to be fallen from jet pipe
Water is online in water cooling tube by sprinkle, and water outlet tubule discharges the underground water after heat exchange.
8. mineral hot furnace as claimed in claim 7 is produced with softened water and recovery system, it is characterised in that：The water cooling pipe network is also
Including upper moisture pipe, one end of upper moisture pipe connects with water outlet tubule, and the other end of upper moisture pipe and the upper hose of make-up tank connect
It is logical, the underground water after heat exchange is delivered in make-up tank, for preparing salt solution.
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|---|---|---|---|
| CN201720734160.8U CN206858217U (en) | 2017-06-22 | 2017-06-22 | Mineral hot furnace is produced with softened water and recovery system |
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| CN201720734160.8U CN206858217U (en) | 2017-06-22 | 2017-06-22 | Mineral hot furnace is produced with softened water and recovery system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107215923A (en) * | 2017-06-22 | 2017-09-29 | 宁夏贺兰山冶金有限公司 | Mineral hot furnace is produced and recovery system with softened water |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107215923A (en) * | 2017-06-22 | 2017-09-29 | 宁夏贺兰山冶金有限公司 | Mineral hot furnace is produced and recovery system with softened water |
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Address after: 753000 north of Shanshui Avenue and west of railway station in Dawukou District, Shizuishan City, Ningxia Hui Autonomous Region Patentee after: Ningxia Lanhu New Material Technology Co.,Ltd. Address before: 753000 north of Shanshui Avenue and west of railway station in Dawukou District, Shizuishan City, Ningxia Hui Autonomous Region Patentee before: NINGXIA HELANSHAN METALLURGY Co.,Ltd. |