Background technology
Currently, the existing import drying cylinder of my one paper machine room of company, oneself uses 4 years, and boiler institute enters drying cylinder for steam
(i.e. paper-making drying cylinder), it is desirable that pressure 1.35MPa, evaporation capacity 10t/h, drying cylinder do not have external water source, and discharge condensed water is through carbonated drink
Separator-water pump-oxygen-eliminating device-feed pump-economizer-boiler drum.Steam-water separator recovered overhead steam is returned through heat pump
It participates in doing work again to drying cylinder.Condensate return accounts for the 60-70% of boiler whole water consumption.It is caused because of brown iron oxide plugging every
Pigging need to be shut down within two months.
Wherein it should be added that:Cylinder iron drying cylinder is used as the critical component that paper is dried to paper machine.It is manufacturing
In quality requirement mustn't have penetrate with excessive sand holes, in order to increase paper smoothness, it is desirable that drying cylinder outer surface polishing and handle
Inner surface Xuan light makes entire cylinder wall keep thickness consistent, and the safety, balance and heat transfer everywhere to ensure drying cylinder are uniform.Drying cylinder
Effect be for drying the moisture in page, ornamenting paper.
It will be apparent that the harm of above-mentioned Ferric oxide scale is very big, it is easy to cause boiler water quality deterioration:Due to boiler inner tubal wall
Corroded, a large amount of iron ion and corrosion product enter boiler, and boiler water quality is caused to deteriorate or take improperly furnace stopping maintenance
Method, when boiler startup, the iron-holder of stove water is up to hundreds of micro- gram per liters, even more than every liter of kilogamma, and the iron-holder of stove water is inclined
Greatly, cyclone separator collapses or misoperation causes steam-water separation not in time, and the iron-holder of steam also can be bigger than normal.
Cause to reduce boiler heat-transfer coefficient or water screen tube overheat:Tube wall uneven heating, amount of scale buildup is different, the higher knot of temperature
Dirt is thicker.Cause fouling corrosion:Heating surface metal is thinning, perforate, Ferric oxide scale is easy to be formed at the high position of thermic load.Pass through
Workshop condensate return flow feedback adjustment effect, on inspection and the discovery oxygen-eliminating device deoxygenation pipeline that consults reference materials is too thin, the row of cannot be satisfied
Oxygen condition opens oxygen-eliminating device safety valve to increase deoxygenation amount, and as a result workshop circling water flow rate is slightly unimpeded, but fails to reach expected effect
Fruit.It will be apparent that the primary structure of existing processing system is only by steam-water separator-water pump-oxygen-eliminating device-feed pump-province
The brief structure such as coal device is constituted, and the water treatment capacity of synthesis is poor, and especially detergent power is poor be easy to cause subsequent pipeline
It blocks.
To sum up, how to overcome the above-mentioned technological deficiency of traditional technology is that the technology that those skilled in the art are badly in need of solving is asked
Topic.
Utility model content
The purpose of this utility model is to provide a kind of paper-making drying cylinders and boiler water cycle processing system, to solve above-mentioned ask
Topic.
In order to achieve the above object, the technical solution of the utility model is realized in:
The utility model provides a kind of paper-making drying cylinder and boiler water cycle processing system, including raw water box 1, raw water pump 2,
Sand filter 3, carbon filter 4, cartridge filter 5, high-pressure pump 6, reverse osmosis unit 7, reverse osmosis produced water tank 8, softened water pump 9, first are soft
Change device 10;
Further include the second demineralizer 11, softened water tank 12, oxygen-eliminating device 13, feed pump 14, economizer 15 and boiler 16;
Wherein, the originally well water pipeline of paper machine room is connect by inlet valve with the raw water box 1;And the raw water box 1,
The raw water pump 2, the sand filter 3, the carbon filter 4, the cartridge filter 5, the high-pressure pump 6, the reverse osmosis dress
It sets the 7, reverse osmosis produced water tank 8, the softened water pump 9, first demineralizer 10 and passes sequentially through a segment pipe sequential communication;
And first demineralizer 10 is also connected to second demineralizer 11;Second demineralizer 11, the soft water
Case 12, the oxygen-eliminating device 13, the feed pump 14, the economizer 15 and the boiler 16 pass sequentially through segment pipe sequence and connect
It is logical.
It preferably, can embodiment as one kind;On pipeline between second demineralizer 11, the softened water tank 12 also
It is provided with production water valve 19.
It preferably, can embodiment as one kind;The top of the softened water tank 12 is provided with plus sodium hydroxide, tertiary sodium phosphate
Addition window.
It preferably, can embodiment as one kind;Oxygen scavenger dosing mouth is provided at the down-comer of the oxygen-eliminating device 13.
It preferably, can embodiment as one kind;The paper-making drying cylinder further includes that water steams with boiler water cycle processing system
Vapour is by gas-distributing cylinder 17 and is sent to steam pipe network 18;The drainage position of the boiler 16 by pipeline successively with the gas-distributing cylinder 17 and
It is described to be sent to the connection of steam pipe network 18.
It preferably, can embodiment as one kind;The top of the gas-distributing cylinder 17 is provided with condensed water and mouth is added.
It preferably, can embodiment as one kind;The bottom of the gas-distributing cylinder 17 is provided with drain valve.
Compared with prior art, it is the advantages of the utility model embodiment:
A kind of paper-making drying cylinder provided by the utility model and boiler water cycle processing system, analyze above-mentioned paper-making drying cylinder and pot
Known to the primary structure of stove water circulation processing system:Above-mentioned paper-making drying cylinder and boiler water cycle processing system its include mainly raw water
It is case 1, raw water pump 2, sand filter 3, carbon filter 4, cartridge filter 5, high-pressure pump 6, reverse osmosis unit 7, reverse osmosis produced water tank 8, soft
Water pump 9, the first demineralizer 10;And second demineralizer 11, softened water tank 12, oxygen-eliminating device 13, feed pump 14, economizer 15 and boiler
The structures such as 16 are constituted;
Wherein, the originally well water pipeline of paper machine room is connect by inlet valve with the raw water box 1;And the raw water box 1,
The raw water pump 2, the sand filter 3, the carbon filter 4, the cartridge filter 5, the high-pressure pump 6, the reverse osmosis dress
It sets the 7, reverse osmosis produced water tank 8, the softened water pump 9, first demineralizer 10 and passes sequentially through a segment pipe sequential communication;
And first demineralizer 10 is also connected to second demineralizer 11;Second demineralizer 11, the soft water
Case 12, the oxygen-eliminating device 13, the feed pump 14, the economizer 15 and the boiler 16 pass sequentially through segment pipe sequence and connect
It is logical.
Paper-making drying cylinder provided by the utility model and boiler water cycle processing system fully utilize sand filter 3, described
The layering of carbon filter 4, the cartridge filter 5 has carried out the filtration treatment of well water;Simultaneously its additionally use high-pressure pump 6,
The devices of the compositions such as reverse osmosis unit 7, reverse osmosis produced water tank 8 realizes reverse osmosis purified treatment, in this way can be to well water into traveling
The thorough purified treatment of comparison of one step;Softened finally by demineralizer, then successively using oxygen-eliminating device 13, feed pump
14, the structures such as economizer 15 and boiler 16, eventually enter into boiler 16 water source will cleaned water source, largely subtract
The formation of impurity in boiler is lacked, water process detergent power is stronger, the problem of blocking which obviate subsequent pipeline.
Specific implementation mode
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model a part of the embodiment, instead of all the embodiments.Based on the embodiments of the present invention, originally
The every other embodiment that field those of ordinary skill is obtained without making creative work, belongs to this practicality
Novel protected range.
In the description of the present invention, it should be noted that the word of the orientation or positional relationship of certain instructions, only
It is the utility model and simplified description for ease of description, spy must be had by not indicating or implying the indicated device or element
Fixed orientation, with specific azimuth configuration and operation, therefore should not be understood as limiting the present invention.
In the description of the present invention, it should be noted that " connection " shall be understood in a broad sense, for example, it may be fixed
Connection, may be a detachable connection, or be integrally connected;It can be mechanical connection, can also be electrical connection;Can be direct
It is connected, can also can is indirectly connected through an intermediary the connection inside two elements.For the ordinary skill of this field
For personnel, the concrete meaning of above-mentioned term in the present invention can be understood with concrete condition.
The utility model is further described in detail below through specific implementation examples and in conjunction with the accompanying drawings.
Referring to Fig. 1, Fig. 2, the utility model embodiment provides a kind of paper-making drying cylinder and boiler water cycle processing system, packet
Include raw water box 1, raw water pump 2, sand filter 3, carbon filter 4, cartridge filter 5, high-pressure pump 6, reverse osmosis unit 7, reverse osmosis produced water
Case 8, softened water pump 9, the first demineralizer 10;
Further include the second demineralizer 11, softened water tank 12, oxygen-eliminating device 13, feed pump 14, economizer 15 and boiler 16;
Wherein, the originally well water pipeline of paper machine room is connect by inlet valve with the raw water box 1;And the raw water box 1,
The raw water pump 2, the sand filter 3, the carbon filter 4, the cartridge filter 5, the high-pressure pump 6, the reverse osmosis dress
It sets the 7, reverse osmosis produced water tank 8, the softened water pump 9, first demineralizer 10 and passes sequentially through a segment pipe sequential communication;
And first demineralizer 10 is also connected to second demineralizer 11;Second demineralizer 11, the soft water
Case 12, the oxygen-eliminating device 13, the feed pump 14, the economizer 15 and the boiler 16 pass sequentially through segment pipe sequence and connect
It is logical.
It preferably, can embodiment as one kind;On pipeline between second demineralizer 11, the softened water tank 12 also
It is provided with production water valve 19.
It preferably, can embodiment as one kind;The top of the softened water tank 12 is provided with plus sodium hydroxide, tertiary sodium phosphate
Addition window.
It preferably, can embodiment as one kind;Oxygen scavenger dosing mouth is provided at the down-comer of the oxygen-eliminating device 13.
It preferably, can embodiment as one kind;The paper-making drying cylinder further includes that water steams with boiler water cycle processing system
Vapour is by gas-distributing cylinder 17 and is sent to steam pipe network 18;The drainage position of the boiler 16 by pipeline successively with the gas-distributing cylinder 17 and
It is described to be sent to the connection of steam pipe network 18.
It preferably, can embodiment as one kind;The top of the gas-distributing cylinder 17 is provided with condensed water and mouth is added.
It preferably, can embodiment as one kind;The bottom of the gas-distributing cylinder 17 is provided with drain valve.
Correspondingly, the utility model additionally provides a kind of paper-making drying cylinder and boiler water cycle processing method, including grasps as follows
Make step:
The originally well water pipeline of paper machine room is connect by inlet valve with raw water box 1, then by raw water pump 2 after, successively
Antisludging agent is added, through pipeline by cartridge filter 5, is passed through later after carbon filter 4 removes solid impurity by sand filter 3
High-pressure pump 6 pressurizes, and reverse osmosis operation is carried out in reverse osmosis unit 7, reverse osmosis produced water tank 8 is then stored water in and is delayed
It deposits, the first demineralizer 10 is sent to by softened water pump 9 later, after being softened;
It is sent to softened water tank 12, addition sodium hydroxide, tertiary sodium phosphate are handled in softened water tank 12, later send water
Toward oxygen-eliminating device 13, in oxygen-eliminating device 13 drugs such as oxygen scavenger are added carries out deoxygenation, then by feed pump 14 be sent to economizer 15,
Boiler 16, is heated, and waits until that water vapour, water vapour are sent to steam pipe network 18 by gas-distributing cylinder 17;
It is needed in gas-distributing cylinder 17 through condensed water dosing.
It should be noted that;It is another to need to pay attention to following aspects:Using adding oxygen scavenger, steam at 13 down-comer of oxygen-eliminating device
Pipeline adds steam condensate (SC) inorganic agent;13 safety valve of oxygen-eliminating device is closed, 13 make-up water of oxygen-eliminating device (softened water+return water) stops steam
Heating and deoxygenation, maintain the temperature at 80-90 DEG C or more.Before dosing using colorimetric determination to oxygen-eliminating device dissolved oxygen >=
0.1mgO2/l, dissolved oxygen meter detection:1.40mgO2/l.In stove plus the bucket of sodium hydroxide, tertiary sodium phosphate should clean up, and special bucket is special
With with soft water or mixing water dissolution addition.Thorough backwash in 3-5 days 1 time after sand filter 3, carbon filter 4 work, input makes after just washing
With.
Reverse osmosis equipment forbids 1 anhydrous startup of raw water box, winter must be antifreeze, carries out Insulation.First demineralizer 10,
Two demineralizers 11 have supervised the detection of hardness, control the recovery time, just wash the time, cannot have chlorion to enter boiler system.
Reagent management:Using label on preceding good reagent and suction pipe, mistake is forbidden to take, should whip lid after taking wrong reagent, standard solution to take
Good bottle cap, must not be open in air;If suction pipe pollution takes wrong reagent, is please rinsed only with soft water, cleaned with clean paper, used
When with reagent clean two times suction pipes.Chemical deoxidizing long-term economic is run, and also there are certain requirements to feed temperature, 60 DEG C of water temperature with
Under, it needs that dosage is turned up according to temperature, the higher temperature the more economical.
The paper-making drying cylinder that the utility model embodiment provides has the technology of following aspect with boiler water cycle processing system
Advantage:
One, the paper-making drying cylinder and boiler water cycle processing system, structure design that the utility model embodiment provides more close
Reason;Wherein, paper-making drying cylinder and boiler water cycle processing system include raw water box, raw water pump, sand filter, carbon filter, security personnel's filtering
Device, high-pressure pump, reverse osmosis unit, reverse osmosis produced water tank, softened water pump, the first demineralizer;Further include the second demineralizer, softened water tank,
Oxygen-eliminating device, feed pump, economizer and boiler etc. structure;It will be apparent that above-mentioned raw water box, raw water pump, sand filter, carbon filter, guarantor
Pacify filter, high-pressure pump, reverse osmosis unit, reverse osmosis produced water tank, softened water pump, the first demineralizer;Further include the second demineralizer, soft
Connection relation and position relationship between the concrete structures such as water tank, oxygen-eliminating device, feed pump, economizer and boiler have reasonably
Layout designs;Therefore the paper-making drying cylinder and boiler water cycle processing system that the utility model embodiment provides, technical construction is more
Rationally, and function is more perfect, and practicability is also stronger.
Two, the paper-making drying cylinder and boiler water cycle processing system that the utility model embodiment provides, largely
Reduce the formation of impurity in boiler, water process detergent power is stronger, the problem of blocking which obviate subsequent pipeline.
Three, the paper-making drying cylinder and boiler water cycle processing system that the utility model embodiment provides, apply complicated pipe
Road is designed, and space structure arrangement is more reasonable;There is good purification simultaneously, the technical advantages such as performance is reliable and stable.
Based on above many significant technical advantages, paper-making drying cylinder provided by the utility model and boiler water cycle processing system
System, will bring good market prospects and economic benefit.
Finally it should be noted that:The above various embodiments is only to illustrate the technical solution of the utility model, rather than limits it
System;Although the utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art should
Understand:It still can be with technical scheme described in the above embodiments is modified, either to which part or whole
Technical characteristic carries out equivalent replacement;And these modifications or replacements, this practicality that it does not separate the essence of the corresponding technical solution are new
The range of each embodiment technical solution of type.