CN204342448U - A kind of production system of bentonite sodium modification - Google Patents
A kind of production system of bentonite sodium modification Download PDFInfo
- Publication number
- CN204342448U CN204342448U CN201420601580.5U CN201420601580U CN204342448U CN 204342448 U CN204342448 U CN 204342448U CN 201420601580 U CN201420601580 U CN 201420601580U CN 204342448 U CN204342448 U CN 204342448U
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- raw material
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- bentonite
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Abstract
The utility model discloses a kind of production system of bentonite sodium modification, comprising: ore deposit soil raw material storage, forklift, rotary conveyor, rotary drying machine, fluidizing furnace, dust-removal system, raw material storage, screw conveyor, sodium carbonate storehouse, electronic scales, Raymond mill, hurricane powder collector, whirly fly-ash separator, finished product lift, stockyard and wrapping machine; Omnidistance by conputer controlled, electronic scales by ore deposit soil and sodium carbonate in fill a prescription in ratio under expect in Raymond mill feeding auger, feeding Raymond mill is mixed and finely ground, and requires that fineness is at 200-300 order, sends into homogenizing in stockyard react by lift, produce sodium-ionized bentonite, pack warehouse-in by wrapping machine, the advantages such as its feature has above fresh water pulping light weight, mud Pulp suspension, the solid wall of drilling well is functional, and oilness is good, rig load can be alleviated, can widely popularize.
Description
Technical field
The utility model relates to a kind of production system of bentonite sodium modification, belongs to wilkinite production technical field.
Background technology
The wilkinite of existing most domestic, when for all kinds of drilling well, is made mud Pulp by what is said or talked about water, is used for drilling well Gu Bi, just produces solids precipitation, again need stir and could use, take a lot of work very much after common bentonite in powder pulping within very short time, time-consuming, etc. shortcoming.
Summary of the invention
Problem to be solved in the utility model is to provide a kind of production system of bentonite sodium modification.
In order to solve the problems of the technologies described above, the production system of the bentonite sodium modification that the utility model provides comprises: swelling ore deposit soil raw material storage, forklift, rotary conveyor, rotary drying machine, fluidizing furnace, dust-removal system, raw material storage, screw conveyor, sodium carbonate storehouse, electronic scales, Raymond mill, hurricane powder collector, whirly fly-ash separator, finished product lift, stockyard and wrapping machine; It is characterized in that: omnidistance by conputer controlled, the material of ore deposit soil raw material storage installs on rotary conveyor by forklift, ore deposit soil is sent in rotary drying machine by conputer controlled rotary conveyor, fluidizing furnace is in rotary drying machine indirect heating, the outlet of fluidizing furnace is connected with dust-removal system, the steam produced in rotary drying machine by vacuum fan discharged to dust-removal system, flue dust after dedusting discharged to chimney; The ore deposit soil of drying is sent to raw material storage homogenizing by lift, ore deposit soil is sent to Raymond mill hopper by screw conveyor by raw material storage outlet, require that the ore deposit soil water ratio after drying homogenizing is in 2-3 ﹪, electronic scales by sodium carbonate in formula in ratio under expect in Raymond mill feeding auger, enter Raymond mill to be mixed and finely ground, require that fineness is at 200-300 order, send into homogenizing in stockyard by lift and react, generate sodium-ionized bentonite, pack warehouse-in by wrapping machine.Its feature has the advantages such as fresh water pulping light weight, Ni Pulp suspension surface, the solid wall of drilling well be functional, and oilness is good, can alleviate rig load.
Ratio sodium carbonate is 0.02-0.04.
Dry the ore deposit soil water ratio after homogenizing in 2-3 ﹪.
Require that sodium-ionized bentonite fineness is at 200-300 order.
The sodium-ionized bentonite adopting technique scheme to produce, has following progress compared with common wilkinite: 1. fresh water pulping light weight ， Ni Pulp energy suspension surface; 2. Ni Pulp can keep the strong state that suspends lastingly, does not precipitate; 3. the solid wall of drilling well is functional; 4. lubricity is good, can alleviate rig load, is to put to obtain the good production method of a kind of bentonite sodium modification of promoting.
In sum, the utility model is a kind of production method of energy Na-modified Bentonite, by bentonite sodium modification, can improve lubricity, fresh water pulping light weight, Ni Pulp suspension surface, the solid wall of drilling well are functional, use cost can be reduced, improve work efficiency, reduce artificial, improve drilling speed, reduction of erection time, its production method is simple.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Accompanying drawing is the utility model production-process systems schematic diagram.
In figure: 1. ore deposit Tu Ku, 2. forklift, 3. conveyor, 4. rotary drying machine, 5. dust-removal system, 6. induced draft fan, 7. fluidizing furnace, 8. chimney, 9. lift, 10. raw material storage, 11. screw conveyors, 12. electronic scaless, 13. sodium carbonate storehouses, 14. Raymond mills, 15. whirly fly-ash separators, 16. hurricane powder collectors, 17. gas blowers, 18. finished product lifts, 19 stockyards, 20. wrapping machines.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
See accompanying drawing, the production system of bentonite sodium modification comprises: swelling ore deposit soil raw material storage 1, forklift 2, rotary conveyor 3, rotary drying machine 4, fluidizing furnace 7, dust-removal system 5, induced draft fan 6, chimney 8, lift 9, raw material storage 10, screw conveyor 11. electronic scales 12, sodium carbonate storehouse 13, Raymond mill 14, whirly fly-ash separator 15, Raymond mill hurricane powder collector 16, gas blower 17, finished product lift 18, stockyard 19 and wrapping machine 20; It is characterized in that: the discharge end of rotary conveyor 3 is connected with the feed end of rotary drying machine 4, the discharge end of rotary drying machine 4 is connected with lift 9 import of raw material cabin 10; Fluidizing furnace 7 is in the indirect heating of rotary drying machine 4, the vapour pipe that fluidizing furnace 7 flue outlet and the inside of rotary drying machine 4 produce is connected with the blast pipe of dust-removal system 5 simultaneously, the air outlet tube of dust-removal system 5 is connected with the blast pipe of induced draft fan 6, and air outlet tube is connected with chimney 8; The outlet of lift 9 is connected with the opening for feed of raw material storage 10, the outlet of raw material storage 10 is connected with screw conveyor 11, the outlet in sodium carbonate storehouse 13 is connected with screw conveyor 11, discharge port is connected with Raymond mill opening for feed, Raymond mill air outlet is connected with the blast pipe of hurricane powder collector 16, air outlet tube is connected with gas blower 17 blast inlet, and air outlet tube is connected with Raymond mill blast inlet, and whirly fly-ash separator 15 adjusts gas blower 17 air outlet tube blast; The lower powder mouth of hurricane powder collector 16 is connected with the import of finished product lift 18, and export and be connected with the opening for feed of stockyard 19, discharge port is connected with wrapping machine opening for feed.
During work, ore deposit soil in soil storehouse 1, ore deposit is put in the hopper of rotary conveyor 3 by forklift 2, be fed in rotary drying machine 4 by conputer controlled conveyor 3, the heat that fluidizing furnace 7 produces heats to rotary drying machine 4, drying and dewatering is carried out to wet soil, dirt wind with water vapour from dryer 4 feed end discharge, enter dedusting in dust-removal system 5, by induced draft fan 6 discharged to chimney 8 again discharged in the air; Ore deposit soil through drying and dewatering enters lift 9, be sent to homogenizing cooling (between bulk and fritter moisture content homogenizing) in former PSV 10, ore deposit soil in former PSV 10 is sent in Raymond mill 14 hopper by conputer controlled screw conveyor 11 by screw conveyor 11, the raw material in conputer controlled sodium carbonate storehouse 13 is mixed and finely ground in expecting in screw conveyor 11 to be sent in Raymond mill 14 under the ratio in formula simultaneously, fineness requirement 300-400 order; The finished powder that the hurricane powder collector 16. of Raymond mill 14 exports enters finished product lift 18, and be sent to by powder in stockyard 19 and carry out natridization reaction, whirly fly-ash separator 15 adjusts blast, and the outlet of stockyard 19 packs warehouse-in by wrapping machine 20.This production system, output is high, steady quality, saving of labor, power saving, remarkable in economical benefits, is a kind of good method of bentonite sodium modification, puts promote.
Claims (2)
1. a production system for bentonite sodium modification, comprising: ore deposit soil raw material storage, forklift, rotary conveyor, rotary drying machine, fluidizing furnace, dust-removal system, raw material storage, screw conveyor, sodium carbonate storehouse, electronic scales, Raymond mill, hurricane powder collector, whirly fly-ash separator, finished product lift, stockyard and wrapping machine; It is characterized in that: production system is by conputer controlled, and the material of ore deposit soil raw material storage loads in rotary conveyor hopper by forklift, and rotary conveyor outlet is connected with rotary drying machine import; Fluidizing furnace is in rotary drying machine indirect heating, and the air outlet of fluidizing furnace exports with rotary drying machine and is connected, and rotary drying machine feed end air outlet is connected with fly-ash separator blast inlet, and the air outlet of fly-ash separator is connected with induced draft fan import, and induced draft fan outlet is connected with chimney; Rotary drying machine kiln hood discharge port is connected with lift opening for feed, and lift outlet is connected with raw material cabin import, raw material storage go out bore cross electronic scales metering be connected with screw conveyor import; Going out after bore crosses electronic scales metering of sodium carbonate feed bin is also connected with screw conveyor import, screw conveyor outlet is connected with Raymond mill hopper, the outlet of Raymond mill hurricane powder collector is connected with grog lift opening for feed, and the whirly fly-ash separator of Raymond mill adjusts blast and gathers dust; Grog lift outlet is connected with finished product bin import, and finished product bin outlet is connected with wrapping machine import, packs warehouse-in by wrapping machine.
2. according to claim 1, a kind of production system of bentonite sodium modification, is characterized in that: rotary conveyor is fed in raw material by forklift, sends in rotary drying machine and dries.
3. according to claim 1 or 2, a kind of production system of bentonite sodium modification, it is characterized in that: after ore deposit soil utilizes rotary drying machine to dry, under the ratio in formula, ore deposit soil and sodium carbonate are expected in screw conveyor that being sent to Raymond mill is mixed and finely ground by conputer controlled electronic scales.
4. according to claim 1, a kind of production system of bentonite sodium modification, is characterized in that: the ore deposit soil after oven dry sends into homogenizing in raw material storage by lift.
5. according to claim 1 or 4, a kind of production system of bentonite sodium modification, is characterized in that: the finished powder after levigate sends into natridization reaction in stockyard by lift, generates sodium-ionized bentonite, packs warehouse-in by wrapping machine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420601580.5U CN204342448U (en) | 2014-10-17 | 2014-10-17 | A kind of production system of bentonite sodium modification |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420601580.5U CN204342448U (en) | 2014-10-17 | 2014-10-17 | A kind of production system of bentonite sodium modification |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204342448U true CN204342448U (en) | 2015-05-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420601580.5U Expired - Fee Related CN204342448U (en) | 2014-10-17 | 2014-10-17 | A kind of production system of bentonite sodium modification |
Country Status (1)
| Country | Link |
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| CN (1) | CN204342448U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110339931A (en) * | 2019-08-14 | 2019-10-18 | 中交（天津）生态环保设计研究院有限公司 | A kind of moveable river and lake dredging soil Flour milling method of modularization, system and technique |
| CN117308536A (en) * | 2023-12-01 | 2023-12-29 | 山东雍联新材料科技有限公司 | Sodium-modified drying rotary furnace for calcium bentonite |
-
2014
- 2014-10-17 CN CN201420601580.5U patent/CN204342448U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110339931A (en) * | 2019-08-14 | 2019-10-18 | 中交（天津）生态环保设计研究院有限公司 | A kind of moveable river and lake dredging soil Flour milling method of modularization, system and technique |
| CN117308536A (en) * | 2023-12-01 | 2023-12-29 | 山东雍联新材料科技有限公司 | Sodium-modified drying rotary furnace for calcium bentonite |
| CN117308536B (en) * | 2023-12-01 | 2024-02-09 | 山东雍联新材料科技有限公司 | Sodium-modified drying rotary furnace for calcium bentonite |
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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: 20150520 Termination date: 20191017 |