CN202175596U - Combined water treatment equipment integrating functions of deoxidization and sodium ion exchange - Google Patents

Combined water treatment equipment integrating functions of deoxidization and sodium ion exchange Download PDF

Info

Publication number
CN202175596U
CN202175596U CN2011202551320U CN201120255132U CN202175596U CN 202175596 U CN202175596 U CN 202175596U CN 2011202551320 U CN2011202551320 U CN 2011202551320U CN 201120255132 U CN201120255132 U CN 201120255132U CN 202175596 U CN202175596 U CN 202175596U
Authority
CN
China
Prior art keywords
water
deoxidization
water tank
deoxygenation
sodium ion
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.)
Expired - Fee Related
Application number
CN2011202551320U
Other languages
Chinese (zh)
Inventor
李运玮
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SHANDONG SHUIFA ENVIRONMENT TECHNOLOGY CO., LTD.
Original Assignee
SHANDONG JINGLU WATER GROUP Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SHANDONG JINGLU WATER GROUP Co Ltd filed Critical SHANDONG JINGLU WATER GROUP Co Ltd
Priority to CN2011202551320U priority Critical patent/CN202175596U/en
Application granted granted Critical
Publication of CN202175596U publication Critical patent/CN202175596U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Treatment Of Water By Ion Exchange (AREA)

Abstract

The utility model provides combined water treatment equipment with the functions of deoxidization and sodium ion exchange, and belongs to the field of water treatment equipment. The combined water treatment equipment structurally comprises a sodium ion exchanger, a demineralized water tank, a deoxidization water pump, a filtration-type deoxidization device and a deoxidized water tank, wherein the water inlet pipe of the sodium ion exchanger is connected with a raw water source, the water outlet pipe of the sodium ion exchanger is connected with the water inlet pipe of the demineralized water tank, the water outlet pipe of the demineralized water tank is connected in series with the deoxidization water pump and then connected with the water inlet pipe of the filtration-type deoxidization device, the water outlet pipe of the filtration-type deoxidization device is connected with the water inlet pipe of the deoxidized water tank, and a boiler feed pump is arranged on the water outlet pipe of the deoxidized water tank. The combined water treatment equipment can achieve the effect of deoxidization at room temperature without needing to heat the inlet water, ensures stable and reliable deoxidization effect, controls the concentration of dissolved oxygen in the effluent less than or equal to 0.05 mg/L to meet the water quality standards for low-pressure boilers, completes water demineralization with high automation degree, and can be widely applied to industrial boilers, heat exchangers, air conditioners, laundry equipment and bath equipment and applied in the food, pharmaceutical and electronic industries.

Description

Have the combined water treatment equipment of deoxygenation and sodium ion function of exchange concurrently
Technical field
The utility model relates to a kind of water treating equipment, specifically a kind of combined water treatment equipment that has deoxygenation and sodium ion function of exchange concurrently.
Background technology
The feedwater of boiler has strict requirement, at first needs to handle through softening or desalination, makes not scaling of boiler surface inside.But, still containing oxygen and other gases in the water, oxygen is a kind of main depolarizer; Can cause boiler plant and therrmodynamic system metal covering to produce corrosion, this corrosion often is the corrosion of locality ulcer, causes the metallic walls perforation when serious; Not only shorten the life-span of boiler plant greatly; And influence the security of boiler and therrmodynamic system, therefore, must adopt how empty iron and oxygen reaction generation Indian red to precipitate.It is filtrate that deoxygenator adopts sponge iron, and tank body is designed to two backwash structures, and the reactant of filtrate and trapped substance can be washed away fully.
Na-ion exchanger is the brand-new soft water disposal system and method for a kind of environmental protection, economy, safety.With terminal user's requirement is principle of design, and in conjunction with former water pretreatment, the WQM mixing system is selected novel essence to set and formed full automatic sodium ion exchange soft water system fully.Great number of issues such as the working cost that the user used water softener separately in the past and caused is high, equipment failure is frequent, effluent quality is unstable, customer need water quality does not match have thoroughly been solved.Having obtained user's in all parts of the country extensive approval, is client's optimal selection.
Summary of the invention
The technical assignment of the utility model is the deficiency to prior art, and a kind of combined water treatment equipment that has deoxygenation and sodium ion function of exchange concurrently is provided.
The utility model solves the technical scheme that its technical problem adopted:
Sponge iron has huge specific surface area, is spongy mushy abrasive grit, and inner porous is netted, and specific surface area for the dissolved oxygen in the water provides great reaction compartment, has been quickened the carrying out of redox reaction greater than 80m2/g.When the water that contains dissolved oxygen passed through sponge iron, oxidizing reaction completely took place in water oxygen gas and iron, thereby guaranteed that the water outlet dissolved oxygen content is lower than below 0.05 mg/L, and its reaction formula is: 2Fe+2H2O+O2 → 2Fe (OH) 2.Fe (OH) 2 is adsorbed on the sponge iron particle, but it is unsettled in oxygen-containing water, and it will be oxidized to ferric compound, and its reaction formula is: 4Fe (OH) 2+2H2O+O2 → 4Fe (OH) 3.Reaction product Fe (OH) 3 is water-fast yellow-green colour flocks, is intercepted in the sponge iron particle, when it runs up to a certain degree, just can rinse well with the backwash water of certain intensity, returns to initial deoxygenation ability.
Water hardness mainly is made up of wherein positively charged ion, calcium (Ca2+), magnesium (Mg2+) ion.When the former water that contains hardness passed through the resin layer of interchanger, the calcium in the water, mg ion were discharged sodium ion simultaneously by resin absorption; Effusive water is exactly the softening water that has removed hardness ions in the interchanger like this; After resin absorption calcium, mg ion reach certain saturation ratio, go out water hardness and increase, this moment, water softener can carry out the reproduction operation of exhausted resin automatically according to preset program; Utilize sodium chloride solution (salt solution) through resin, make the resin of inefficacy return to sodium type resin again.
Have the combined water treatment equipment of deoxygenation and sodium ion function of exchange concurrently; Comprise Na-ion exchanger, softening water tank, deoxygenation water pump, filtering type deoxygenator and deoxygenation water tank; The water inlet pipe of Na-ion exchanger connects former water; The rising pipe of Na-ion exchanger connects the water inlet pipe of softening water tank, is connected with the water inlet pipe of filtering type deoxygenator behind the rising pipe series connection deoxygenation water pump of softening water tank, and the rising pipe of filtering type deoxygenator connects the water inlet pipe of deoxygenation water tank.
Above-mentioned deoxygenation water pump has two, is the parallel connection relation and is connected on the rising pipe of softening water tank.
The rising pipe of above-mentioned deoxygenation water tank is provided with boiler feedpump, and boiler feedpump has two, is the parallel connection relation and is connected on the rising pipe of deoxygenation water tank.
The combined water treatment equipment that has deoxygenation and sodium ion function of exchange concurrently of the utility model compared with prior art, the beneficial effect that is produced is:
1) can realize deoxygenation at normal temperatures, water inlet need not heating; Deaerating effect is reliable and stable, and dissolved oxygen content is stablized≤0.05mg/L in the water outlet, meets the low pressure boiler water quality standard;
2) but the equipment low level arranges that technology is simple, no too high requirement for height; The flow process advantages of simple, simple and compact equipment structure, easy handling is safeguarded;
3) level of automation is high, and equipment can carry out back flushing according to time or work crushing automatically, need not manual operation, and back flushing has timely been eliminated oxygen scavenger caking situation, reduced the water consumption, makes equipment be in good working order all the time;
4) water demineralization process automation: this equipment is realized the robotization of IX and resin regeneration process through programcontrol unit;
5) suitability is wide: can be used for industries such as Industrial Boiler, heat exchanger, air-conditioning, laundry, shower equipment and food, pharmacy, electronics. 
Description of drawings
Accompanying drawing 1 is the structural representation of the utility model. 
Among the figure, 1, Na-ion exchanger, 2, softening water tank, 3, the deoxygenation water pump, 4, the filtering type deoxygenator, 5, the deoxygenation water tank, 6, boiler feedpump.
Embodiment
Below in conjunction with explanation at length below the combined water treatment equipment work that has deoxygenation and sodium ion function of exchange concurrently of 1 pair of the utility model of accompanying drawing.
Shown in accompanying drawing 1; The combined water treatment equipment that has deoxygenation and sodium ion function of exchange concurrently of the utility model; Its structure comprises Na-ion exchanger 1, softening water tank 2, deoxygenation water pump 3, filtering type deoxygenator 4 and deoxygenation water tank 5; The water inlet pipe of Na-ion exchanger 1 connects former water, and the rising pipe of Na-ion exchanger 1 connects the water inlet pipe of softening water tank 2, and rising pipe series connection deoxygenation water pump 3 backs of softening water tank 2 are connected with the water inlet pipe of filtering type deoxygenator 4; The rising pipe of filtering type deoxygenator 4 connects the water inlet pipe of deoxygenation water tank 5, and the rising pipe of deoxygenation water tank 5 is provided with boiler feedpump 6.
Above-mentioned deoxygenation water pump 3 has two, is the parallel connection relation and is connected on the rising pipe of softening water tank 2.
Above-mentioned boiler feedpump 6 has two, is the parallel connection relation and is connected on the rising pipe of deoxygenation water tank 5.
Its processing and fabricating of combined water treatment equipment that has deoxygenation and sodium ion function of exchange concurrently of the utility model is simple and convenient, and processing and fabricating gets final product shown in the by specification accompanying drawing.The intake pressure of Na-ion exchanger own is no more than 0.3Mpa, and water outlet there is not pressure basically, carries out buffer memory so softening water tank is set; And the required pressure of deoxygenator is 0.3Mpa, the deoxygenation water pump must be set give pressure of deoxygenator. 
Except that the described technical characterictic of specification sheets, be the known technology of those skilled in the art.

Claims (4)

1. have the combined water treatment equipment of deoxygenation and sodium ion function of exchange concurrently; Comprise Na-ion exchanger (1), softening water tank (2), deoxygenation water pump (3), filtering type deoxygenator (4) and deoxygenation water tank (5); It is characterized in that; The water inlet pipe of Na-ion exchanger (1) connects former water; The rising pipe of Na-ion exchanger (1) connects the water inlet pipe of softening water tank (2), and rising pipe series connection deoxygenation water pump (3) back of softening water tank (2) is connected with the water inlet pipe of filtering type deoxygenator (4), and the rising pipe of filtering type deoxygenator (4) connects the water inlet pipe of deoxygenation water tank (5).
2. the combined water treatment equipment that has deoxygenation and sodium ion function of exchange concurrently according to claim 1 is characterized in that above-mentioned deoxygenation water pump (3) has two, is the parallel connection relation and is connected on the rising pipe of softening water tank (2).
3. the combined water treatment equipment that has deoxygenation and sodium ion function of exchange concurrently according to claim 1 is characterized in that the rising pipe of deoxygenation water tank (5) is provided with boiler feedpump (6).
4. the combined water treatment equipment that has deoxygenation and sodium ion function of exchange concurrently according to claim 3 is characterized in that above-mentioned boiler feedpump (6) has two, is the parallel connection relation and is connected on the rising pipe of deoxygenation water tank (5).
CN2011202551320U 2011-07-19 2011-07-19 Combined water treatment equipment integrating functions of deoxidization and sodium ion exchange Expired - Fee Related CN202175596U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011202551320U CN202175596U (en) 2011-07-19 2011-07-19 Combined water treatment equipment integrating functions of deoxidization and sodium ion exchange

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011202551320U CN202175596U (en) 2011-07-19 2011-07-19 Combined water treatment equipment integrating functions of deoxidization and sodium ion exchange

Publications (1)

Publication Number Publication Date
CN202175596U true CN202175596U (en) 2012-03-28

Family

ID=45865491

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011202551320U Expired - Fee Related CN202175596U (en) 2011-07-19 2011-07-19 Combined water treatment equipment integrating functions of deoxidization and sodium ion exchange

Country Status (1)

Country Link
CN (1) CN202175596U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102786120A (en) * 2012-08-30 2012-11-21 陕西师范大学 Normal-temperature normal-pressure water body dissolved oxygen high-gradient magnetic separation continuous removal device
CN106396135A (en) * 2016-09-26 2017-02-15 汪传发 Water softening apparatus and water softening method
CN106673260A (en) * 2016-12-30 2017-05-17 中国石油天然气股份有限公司 Oil and gas field station industrial boiler water and domestic drinking water treatment system and method
CN109399780A (en) * 2018-10-26 2019-03-01 上海同赛水处理科技有限公司 A kind of sponge iron filtering deaerating plant

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102786120A (en) * 2012-08-30 2012-11-21 陕西师范大学 Normal-temperature normal-pressure water body dissolved oxygen high-gradient magnetic separation continuous removal device
CN106396135A (en) * 2016-09-26 2017-02-15 汪传发 Water softening apparatus and water softening method
CN106673260A (en) * 2016-12-30 2017-05-17 中国石油天然气股份有限公司 Oil and gas field station industrial boiler water and domestic drinking water treatment system and method
CN109399780A (en) * 2018-10-26 2019-03-01 上海同赛水处理科技有限公司 A kind of sponge iron filtering deaerating plant

Similar Documents

Publication Publication Date Title
CN105664963B (en) A kind of water process ozone catalyst and preparation method thereof
CN103768907B (en) A kind of method of yellow phosphoric tail gas oxidation alkali cleaning deep purifying
CN103332821B (en) Vitriolated method of wastewater treatment in a kind of dye well intermediate production process
CN202175596U (en) Combined water treatment equipment integrating functions of deoxidization and sodium ion exchange
CN102381691A (en) Preparation method of nano hydroxylapatite adsorbent for absorbing heavy metal ions in waste water
CN103127899B (en) A kind of arsenic-removing adsorption agent-iron copper composite oxides and preparation method thereof
CN102660687A (en) Method for recycling heavy metal resources of stainless steel pickling waste water neutralization sludge
CN103805781A (en) Method for inhibiting organic phosphorus and COD in wastewater discharged from rare earth extraction separation enterprises
CN103721675A (en) Modifying method for cationic surface active agent modified activated carbon and application of cationic surface active agent modified activated carbon
CN101269810A (en) Absorbent charcoal fine purification technique
CN106116004A (en) A kind of steel hydrochloric acid pickling effluent resource reclaims and the processing method of zero-emission
CN206089281U (en) Steel industry sulphuric acid pickling liquid waste's processing recovery system
CN204111495U (en) A kind of high efficiency sewage treatment facility
CN103641207B (en) A kind of Zinc-containing electroplating waste water combined electrolysis groove treatment process
CN106673295A (en) Method for treating high-concentration formaldehyde wastewater
CN201942574U (en) Water-saving membrane separate-quality water supply water purifier
CN103641208B (en) A kind of nickeliferous board wastewater combined electrolysis groove treatment process
CN103523860A (en) Method for removing harmful anions from aqueous solution by adopting Friedel salt or Kuzel salt
CN206089294U (en) Steel industry hydrochloric acid pickling liquid waste's processing recovery system
CN202988881U (en) Waste acid and waste saline water treatment system combining inorganic synthesis with carbon absorption
CN105107362A (en) Method for deep removal of zero valence mercury in mercury smelting flue gas
CN209468236U (en) Zero-emission water circulation system in lead smelt production
CN202643366U (en) Modified sponge iron deoxidizing device
CN202808515U (en) Device for producing purified water by utilizing phosphatizing waste water
CN106086896A (en) Based on the wiring board acidity etching liquid recycling system in heavy metal containing wastewater treatment

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C41 Transfer of patent application or patent right or utility model
TR01 Transfer of patent right

Effective date of registration: 20151130

Address after: 272300 Shandong Province Economic Development Zone Jining City Yutai County

Patentee after: SHANDONG SHUIFA ENVIRONMENT TECHNOLOGY CO., LTD.

Address before: 272300 Shandong Province Economic Development Zone Jining City Yutai County

Patentee before: Shandong Jinglu Water Group Company Limited

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20120328

Termination date: 20170719