CN205676196U - A kind of oilfield sewage treatment device - Google Patents
A kind of oilfield sewage treatment device Download PDFInfo
- Publication number
- CN205676196U CN205676196U CN201620556585.XU CN201620556585U CN205676196U CN 205676196 U CN205676196 U CN 205676196U CN 201620556585 U CN201620556585 U CN 201620556585U CN 205676196 U CN205676196 U CN 205676196U
- Authority
- CN
- China
- Prior art keywords
- resin
- level
- tank
- filter
- valve
- 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
Links
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
Abstract
The utility model discloses a kind of oilfield sewage treatment device, it including one-level resin container, second resin tank, inlet water lifting pumps, regeneration elevator pump, enter to filter grid sets and go out to filter grid sets, is provided with out filter guiding region, resin filter district in one-level resin container from top to bottom and enters to filter grid zone；Wherein, enter to filter grid sets identical with the structure going out to filter grid sets and be separately fixed in filter grid zone and resin filter district, entering to filter grid sets and going out to filter grid sets and all include running through the rotary shaft of one-level resin container tank body and by the fixing some Turbogrid plates on the rotating shaft of support, these Turbogrid plates are arranged in parallel；Resin filter district includes the installing rack being arranged in the middle part of one-level resin container and the resin filter element being fixed in installing rack, the utility model substantially prolongs the efficiency lost resin time in the case that flow of inlet water is constant, and bottom water inlet does not results in too big pumping pressure loss, has saved energy.
Description
Technical field
The utility model relates to technical field of sewage, is specially a kind of oilfield sewage treatment device.
Background technology
Viscous crude field commonly used steam injection heating exploitation method is recovered the oil, and injects water into steam boiler and superheated steam boiler
Obtaining the saturated vapor of HTHP, then inject steam into oil reservoir to improve reservoir temperature and to reduce oil reservoir viscosity,
Finally by oil production equipment, viscous crude is risen to ground.Substantial amounts of high temperature oil-polluted water is in thick oil filling steam heating power recovery process
Produce.In order to economize on resources, high temperature oil-polluted water is generally recycled by current oil field, removes high temperature oil-polluted water
Oil, oil removal purified treatment after obtain high temperature sewage, then carry out sofening treatment and obtain hot mastication sewage, it is directly used in
Produce steam.Wherein, the softening process of high temperature sewage is more complicated, and construction investment and processing cost are high, and being that left and right is whole returns
Receive utilization and process the key factor of technique.
Present domestic each elephant tenderizer has medicament tenderizer and ion-exchange, and part offshore platform uses film
Method.Lime softening method can effectively reduce fouling composition and concentration of suspension in water, and can make the softened work of part water treatment agent
Continuing in return-flow system after skill to recycle, milk of lime reacts with the carbonate hardness composition in water, the CaCO3 of generation indissoluble again
Or Precipitation after Mg (OH) 2.Lime one soda softening technique is divided into cold lime and two kinds of techniques of hot lime.Cold lime softens work
Skill is to carry out chemical reaction under conditions of water is temperature-resistant, and hot lime softening process refers to coolant-temperature gage in the future and improves,
It is close to or higher than boiling point.Two techniques differ primarily in that its reaction speed and the solubility of CaCO3, Mg (OH) 2.Hot lime is soft
Metallization processes is more in hgher efficiency than cold lime softening process.But the pressure needed for hot lime technology is very high, in addition it is also necessary to supplemental heat source pair
Water is heated, and there are some safety problems.Ion-exchange, two-stage strong acid sodium ion exchange resin switching technology contains at height
Being widely used in softening process in salt recovered water, first order resin bed removes major part hardness, second level resin
The hardness being in trace in first order resin bed water outlet is all removed by bed, it is ensured that going out hardness of water is 0mg/L.Use NaCl again
Raw, the method operating cost is relatively low, is therefore used widely, but the commonly used one-level of existing ion-exchange unit two grades is all
Forward water inlet technique, presses resin very real, and backwash does not destroy resin level yet, because the oils containing in oilfield sewage and outstanding
Float is piled up for a long time and be will result in resin and harden, and increases pressure reduction and further results in resin fragmentation, and exchange efficiency is greatly reduced, with
When, a large amount of high saliferous regenerative wastewater that regeneration produces is again the difficult point processing.
Utility model content
The purpose of this utility model is to provide a kind of oilfield sewage treatment device, to solve to propose in above-mentioned background technology
Problem.
For achieving the above object, the following technical scheme of the utility model offer:
A kind of oilfield sewage treatment device, including one-level resin container, second resin tank, inlet water lifting pumps, regeneration elevator pump,
Enter to filter grid sets and go out to filter grid sets, be provided with out filter guiding region, resin filter district in one-level resin container from top to bottom and enter filter
Grid zone；Wherein, grid sets is entered to filter identical with the structure going out to filter grid sets and be separately fixed at into filter grid zone and resin mistake
In filter district, enter to filter grid sets and go out to filter grid sets and all include running through the rotary shaft of one-level resin container tank body and fixed by support
Some Turbogrid plates on the rotating shaft, these Turbogrid plates are arranged in parallel；Resin filter district includes being arranged on one-level resin container
The installing rack at middle part and the resin filter element being fixed in installing rack；Inlet water lifting pumps is divided into three tunnels after water intake ball valve, the
One tunnel is connected bottom one-level resin container through water intaking valve under one-level tank, under the second two grades of tunnel tank at the bottom of liquid feed valve and second resin tank
Portion connects, and the 3rd tunnel is connected with one-level resin container top through clear water Valve for washing, and enterprising through one-level tank upper water-out valve and two grades of tanks
Water valve is connected with second resin tank top；Regeneration elevator pump, after regenerated liquid liquid feed valve, leads up to water intaking valve under one-level tank
Being connected with bottom one-level resin container, another road liquid feed valve under two grades of tanks is connected with second resin pot bottom.
As the utility model further technical scheme, one-level resin container sidewall is provided with the dimension of corresponding installing rack
Repair window.
As the utility model further technical scheme, before water intake ball valve, also has water inlet sample tap, in one-level
Also has one-level tank water outlet sample tap, before tank upper water-out valve under the two grades of tanks being connected with second resin pot bottom after outlet valve also
Have two grades of tank water outlet sample taps.
As the utility model further technical scheme, on one-level tank upper water-out valve and two grades of tanks between water intaking valve
Pipeline, is connected with pollution discharge pond also by scum valve, is connected with pollution discharge pond by one-level tank down blow valve bottom one-level resin container,
Second resin pot bottom is connected with pollution discharge pond by two grades of tank down blow valves.
Compared with prior art, the utility model is by arranging large volume one-level resin container, and fits into filter grid sets
Carry out water velocity water conservancy diversion regulation with going out to filter grid sets, improve in the unit interval while volume taking full advantage of resin container
The operating efficiency of resin filter element, substantially prolongs efficiency lost resin time, and bottom water inlet in the case that flow of inlet water is constant
Do not result in too big pumping pressure loss, save energy.
Brief description
Fig. 1 is the structural representation of a kind of oilfield sewage treatment device of the utility model.
In figure: 1-regenerates elevator pump, 2-inlet water lifting pumps, 3-is intake sample tap, 4-water intake ball valve, 5-regenerated liquid feed liquor
Valve, water intaking valve under 6-one-level tank, 7-one-level tank down blow valve, 8-pollution discharge pond, bis-grades of tank down blow valves of 9-, enter under bis-grades of tanks of 10-
Liquid valve, outlet valve under bis-grades of tanks of 11-, 12-second resin tank, water intaking valve on bis-grades of tanks of 13-, 14-scum valve, 15-one-level tank
Upper water-out valve, 16-one-level tank water outlet sample tap, 17-one-level resin container, 18-goes out to filter grid sets, 19-clear water Valve for washing, and 20-pacifies
Shelving, 21-maintenance window, 22-enters to filter grid sets.
Detailed description of the invention
It is described in more detail below in conjunction with the technical scheme to this patent for the detailed description of the invention.
Referring to Fig. 1, a kind of oilfield sewage treatment device, including the 12nd, one-level resin container the 17th, second resin tank intakes lifting
The 2nd, pump regenerates elevator pump and the 1st, enters to filter grid sets 22 and go out to filter grid sets 18, is provided with out filter from top to bottom and leads in one-level resin container 17
Flow district, resin filter district and enter to filter grid zone；Wherein, grid sets 22 is entered to filter identical with the structure going out to filter grid sets 18 and respectively
It is fixed in filter grid zone and resin filter district, enter to filter grid sets 22 and go out to filter grid sets 18 and all include running through one-level resin container
The rotary shaft of 17 tank bodies and by the fixing some Turbogrid plates 22 on the rotating shaft of support, these Turbogrid plates 2 are parallel to each other and set
Put；Resin filter district includes the installing rack 20 being arranged in the middle part of one-level resin container 17 and the resin filter being fixed in installing rack 20
Core, is provided with the maintenance window 21 of corresponding installing rack 20 on one-level resin container 17 sidewall；
Inlet water lifting pumps 2 is divided into three tunnels after water intake ball valve 4, and the first via is through water intaking valve under one-level tank 6 and a grade resins
Connecting bottom tank 17, under the second two grades of tunnel tank, liquid feed valve 10 is connected bottom second resin tank 12, and the 3rd tunnel is just washed through clear water
Valve 19 is connected with one-level resin container 17 top, and through water intaking valve on one-level tank upper water-out valve 15 and two grades of tanks 13 and second resin tank
12 tops connect.
Regeneration elevator pump 1, after regenerated liquid liquid feed valve 5, leads up to water intaking valve 6 and one-level resin container 17 under one-level tank
Bottom connects, and another road liquid feed valve 10 under two grades of tanks is connected bottom second resin tank 12.
Pipeline between water intaking valve 13 on one-level tank upper water-out valve 15 and two grades of tanks, also by scum valve 14 and pollution discharge pond
Connect, be connected with pollution discharge pond 8 by one-level tank down blow valve 7 bottom one-level resin container 17, bottom second resin tank 12, pass through two
Level tank down blow valve 9 is connected with pollution discharge pond.
Also had water inlet sample tap 3 before water intake ball valve 4, also have one-level tank to go out water sampling before one-level tank upper water-out valve 15
Mouth 16, also has two grades of tank water outlet sample taps under the two grades of tanks being connected with second resin pot bottom after outlet valve 11.
Normal softening flow process: sewage promotes power by inlet water lifting pumps 2, by water intake ball valve 4, water intaking valve under one-level tank
6 entrance one-level resin containers 17, control into filter grid sets 22 and the incline direction going out to filter grid sets 18, extend resin ion exchange
Unit effective time, after ion exchange completes, by one-level tank upper water-out valve 15, on two grades of tanks, water intaking valve 13 is entered two grades by upper
Resin container 12, is carried out further ion exchange in second resin tank, is left by outlet valve 11 under two grades of tanks with resin in tank
Equipment.
By arranging large volume one-level resin container, and fit into filter grid sets and go out to filter grid sets and carry out water velocity and lead
Stream regulation, improves the operating efficiency of resin filter element in the unit interval while volume taking full advantage of resin container, in water inlet
Substantially prolongs the efficiency lost resin time in the case that flow is constant, and bottom water inlet does not results in too big pumping pressure loss, joint
About energy.
Regeneration flow process: reused by resin regeneration after efficiency lost resin.
One-level tank regenerates: is 1. first vented residual sewage in one-level tank, is naturally emptied into blowdown by one-level tank down blow valve 7
Pond.2. entering regenerated liquid, regenerated liquid promotes power by regenerating elevator pump 1, by regenerated liquid liquid feed valve 5, then by under one-level tank
Water intaking valve 6 is by lower entrance one-level resin container 17, and regenerated liquid and resin carry out regenerant ions exchange, by one-level tank at low flow rates
Upper water-out valve 15, scum valve 203 enters pollution discharge pond, after regeneration completes, in tank regenerated liquid by one-level tank down blow valve 7 by
Gravity is emitted into pollution discharge pond.3. clear water drip washing after softening, the clear water after softening through resin passes through inlet water lifting pumps 2, water intake ball valve
4, after clear water Valve for washing 19 is by upper entrance one-level resin container 17 drip washing, water enters pollution discharge pond by one-level tank down blow valve 7.
Two grades of tank regeneration: the 1st, backwash, resin container carrys out liquid and passes through inlet water lifting pumps 2, water intake ball valve 4, liquid feed valve under two grades of tanks
10 backwashes enter second resin tank, rinse out residual mechanical impurity in resin bed, and water intaking valve 13 on two grades of tanks is passed through in water outlet, on
Blowoff valve 14 enters pollution discharge pond.2nd, be first vented residual sewage in second resin tank, by two grades of tank down blow valve 9 gravity empty into
Pollution discharge pond.3rd, entering regenerated liquid, regenerated liquid promotes power by regenerating elevator pump 1, by regenerated liquid liquid feed valve 5, enters under two grades of tanks
Liquid valve 10 enters two grades of tanks, and regenerated liquid and resin carry out regenerant ions exchange at low flow rates, by water intaking valve 13 on two grades of tanks,
Scum valve 14 enters pollution discharge pond, and after regeneration completes, in tank, regenerated liquid is emitted into blowdown by two grades of tank down blow valves 9 by gravity
Pond.4th, soften clear water drip washing, soften clear water and pass through inlet water lifting pumps 2, water intake ball valve 4, clear water Valve for washing 19, one-level tank upper water-out
Valve 15, enters pollution discharge pond by two grades of tank down blow valves 9 after water intaking valve 13 enters two grades of tank drip washing on two grades of tanks.
Above the better embodiment of this patent is explained in detail, but this patent is not limited to above-mentioned embodiment party
Formula, in the ken that one skilled in the relevant art is possessed, can also be on the premise of without departing from this patent objective
Various changes can be made.
Claims (4)
1. an oilfield sewage treatment device, it is characterised in that include one-level resin container, second resin tank, inlet water lifting pumps, again
Give birth to elevator pump, enter to filter grid sets and go out to filter grid sets, in one-level resin container, be provided with out filter guiding region, resin filter from top to bottom
District and enter to filter grid zone；Wherein, grid sets is entered to filter identical with the structure going out to filter grid sets and be separately fixed at into filter grid zone
With resin filter district, enter to filter grid sets and go out to filter grid sets and all include running through the rotary shaft of one-level resin container tank body and pass through
The fixing some Turbogrid plates on the rotating shaft of support, these Turbogrid plates are arranged in parallel；Resin filter district includes being arranged on one
Installing rack in the middle part of grade resins tank and the resin filter element being fixed in installing rack；Inlet water lifting pumps is divided into after water intake ball valve
Three tunnels, the first via is connected bottom one-level resin container through water intaking valve under one-level tank, liquid feed valve and two grades under the second two grades of tunnel tank
Connecting bottom resin container, the 3rd tunnel is connected with one-level resin container top through clear water Valve for washing, and through one-level tank upper water-out valve and two
On level tank, water intaking valve is connected with second resin tank top；Regeneration elevator pump, after regenerated liquid liquid feed valve, leads up to one-level tank
Lower water intaking valve is connected bottom one-level resin container, and another road liquid feed valve under two grades of tanks is connected with second resin pot bottom.
2. a kind of oilfield sewage treatment device according to claim 1, it is characterised in that set on one-level resin container sidewall
There is the maintenance window of corresponding installing rack.
3. a kind of oilfield sewage treatment device according to claim 1, it is characterised in that also had before water intake ball valve into
Water sampling mouth, also has one-level tank water outlet sample tap, at two grades be connected with second resin pot bottom before one-level tank upper water-out valve
Two grades of tank water outlet sample taps are also had after outlet valve under tank.
4. a kind of oilfield sewage treatment device according to claim 1, it is characterised in that one-level tank upper water-out valve and two grades
On tank, the pipeline between water intaking valve, is connected with pollution discharge pond also by scum valve, by row under one-level tank bottom one-level resin container
Dirty valve is connected with pollution discharge pond, and second resin pot bottom is connected with pollution discharge pond by two grades of tank down blow valves.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620556585.XU CN205676196U (en) | 2016-06-08 | 2016-06-08 | A kind of oilfield sewage treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620556585.XU CN205676196U (en) | 2016-06-08 | 2016-06-08 | A kind of oilfield sewage treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205676196U true CN205676196U (en) | 2016-11-09 |
Family
ID=57434288
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620556585.XU Expired - Fee Related CN205676196U (en) | 2016-06-08 | 2016-06-08 | A kind of oilfield sewage treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205676196U (en) |
-
2016
- 2016-06-08 CN CN201620556585.XU patent/CN205676196U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101829610A (en) | Water softener regeneration | |
| CN104030496B (en) | A kind of dense oil extraction wastewater degree of depth sofening treatment reuse method | |
| CN100427209C (en) | Duel compartment coagulation mixed beds external regeneration knockout tower and regeneration art work | |
| CN205676196U (en) | A kind of oilfield sewage treatment device | |
| CN205874094U (en) | Online water quality processing system of cogeneration of heat and power heat supply pipe network | |
| CN207091116U (en) | A kind of full-automatic removal water hardness device | |
| CN105858809B (en) | A kind of ion exchange resin continuous regeneration set and ion exchange resin continuous regeneration method | |
| CN105903499B (en) | Ion exchange tower acid-alkali regeneration waste water reuse system and reuse method | |
| CN107971047A (en) | A kind of industrial soft water acid-alkali regeneration liquid recycling method and device | |
| CN2928227Y (en) | External regeneration separating tower for double middle row concrete bed | |
| CN104528877B (en) | Water-cooling circulating system | |
| CN201660466U (en) | Online recycling and treatment system for electroplating waste water containing heavy metal ions | |
| CN207628433U (en) | Backwash resin tower is exempted from a kind of resin regeneration | |
| CN102631955A (en) | Restoration method for removing iron pollution of anion exchange resin and restoration drug formula | |
| CN204125208U (en) | A kind of high temperature oily(waste)water ion exchange softening treatment unit | |
| CN106745512A (en) | Uphole steam generator regenerating softener waste water zero discharge device and its renovation process | |
| CN101264954B (en) | Multi-standard type ion-exchanger | |
| CN207619159U (en) | A kind of condensate polishing treatment regenerative wastewater ammonia recovery system | |
| CN103288171B (en) | Water softening treatment device and regeneration method of softener | |
| CN204958468U (en) | Oil field sewage softening installation | |
| CN205687612U (en) | A kind of ion exchange resin continuous regeneration set | |
| CN104743684B (en) | A kind of industrial sewage recycle and reuse system | |
| CN206156902U (en) | Water supply system for boiler | |
| CN204237642U (en) | A kind of special purpose device of Coal Chemical Industry haline water purification process technique | |
| CN205856191U (en) | A kind of processing system preparing boiler feedwater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20161109 Termination date: 20170608 |