CN1186882A - Direct cooling and cleaning method for dyeing machine - Google Patents

Direct cooling and cleaning method for dyeing machine Download PDF

Info

Publication number
CN1186882A
CN1186882A CN96112918A CN96112918A CN1186882A CN 1186882 A CN1186882 A CN 1186882A CN 96112918 A CN96112918 A CN 96112918A CN 96112918 A CN96112918 A CN 96112918A CN 1186882 A CN1186882 A CN 1186882A
Authority
CN
China
Prior art keywords
dyeing machine
cooling
cleaning
dyeing
pressure
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.)
Pending
Application number
CN96112918A
Other languages
Chinese (zh)
Inventor
林清传
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN96112918A priority Critical patent/CN1186882A/en
Publication of CN1186882A publication Critical patent/CN1186882A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Treatment Of Fiber Materials (AREA)

Abstract

Based on available dyeing machine, the present invention modifies the heat exchanger and exhausting parts of dyeing machine and combines its direct cooling and cleaning parts. The present invention can overcome the demerits of available technology and reach the aims of saving energy, lowering cost and raising product quality.

Description

Direct cooling and cleaning method for dyeing machine
What the present invention relates to is direct cooling and cleaning method for dyeing machine, concretely, the present invention relates to be with the direct cooling of dyeing machine with clean a kind of method that merges; The present invention is the improvement of corresponding exhaust dyeing peripheral devices.
The heating of the exhaust dyeing machine of prior art or the type of cooling are to utilize the indirect heat transfer mode of shell-and-tube exchanger to reach needed dyeing temperature, the indirect mode is for dyeing course, it is the bath of dye liquor ratio that can not influence dyeing course that a very important advantage is arranged, therefore in dyeing course, for fixing bath raio, generally all adopt the indirect mode to come heating-cooling; It is lower that yet the shortcoming of indirect mode is a heat exchanger effectiveness; Therefore with processes such as the irrelevant cooling of bath raio and cleaning in, the purpose of utilizing the indirect mode to reach cooling and cleaning again will waste energy and the time.
The objective of the invention is to dyeing machine directly be cooled off and cleaning merging method, thereby overcome the defective that exists in the prior art by a kind of.
Be description of drawings below, in conjunction with the accompanying drawings, can clearly understand method of the present invention.
Accompanying drawing 1 is the dyeing machine dye liquor circulation of prior art and the schematic diagram of cooling circuit;
Accompanying drawing 2 is schematic diagrames of circuit in the direct cooling and cleaning method for dyeing machine of the present invention (2) (4);
Accompanying drawing 3 is schematic diagrames of circuit in the direct cooling and cleaning method for dyeing machine of the present invention (2) (5);
Below in conjunction with accompanying drawing the present invention is carried out detailed narration.
During normal dyeing, the endless form of dye liquor such as the route among Fig. 1 (1) carry out, That is, dye liquor is discharged from the bottom drain 16 of overflow dyeing machine 9, enters pump along circuit (1) 13, by pump 13 input filters 14, enter then heat exchanger 11, hand over by heat The dye liquor that changes continues to enter along circuit 1 head 8 of overflow dyeing machine 9; When needing cooling, cold But water carries out heat and hands over from water inlet 17 by water pump 12 or directly enter heat exchanger 11 (2) in water after changing such as the accompanying drawing 1, (3) route carry out, and what the port of export 18 flowed out is Callable warm water.
When needing heating, by feeding steam in vapor interface 19 heat exchanger 11, waste heat can be from waste heat recovery mouth 20 recovery waste heats.
Yet in the cooling procedure after dyeing is finished, just need not carry out in mode so, adopt method of the present invention this moment, just can reach the time that shortens cooling and cleaning process, and the energy using water wisely, cut down the consumption of energy.
Method of the present invention is that the endless form of dye liquor such as (1) route in the accompanying drawing 1 are carried out, and (2) in the cold water of heat exchanger 11 such as the accompanying drawing 2, (4) route are advanced; Or cooling water is carried out along (2) in the accompanying drawing 3, (5) route, and as the hydraulic pressure deficiency, then must add a water pump 12, to increase hydraulic pressure, as shown in Fig. 1,2,3, in addition, visible forcing press 15 from accompanying drawing.
When the dye liquor in the dyeing machine 9 arrives the setting liquid level, this setting liquid level has fluid level controller 10 controls, then by the floss hole in the accompanying drawing (6) or (7) discharging dye liquor, when liquid level is hanged down in the arrival of the dye liquor in the dyeing machine 9 setting, then stop discharging, replenish cooling water in dye liquor, the circulation that so goes round and begins again arrives till the chilling temperature that sets always.
Because clean cold water is complemented among the dyeing machine 9 by the circuit in the accompanying drawing 2 (2) (4) or by the circuit in the accompanying drawing 3 (2) (5) always, when so the cooling action is finished, the action of cleaning is also and then finished, later cleaning action no longer needs at all, even need to clean, also the cleaning of manying that just comes briefly than original cleaning process.
Thus, cleaning process has been omitted (because cooling and cleaning process have combined), reaches the purpose of shortening processing procedure time, using water wisely, conserver power source naturally.
What deserves to be mentioned is that in cooling and cleaning merging process, most dye liquor impurity has also emitted together, because therefore dye liquor impurity partly, utilize method of the present invention can improve dyeing quality discharging in the cooling indirectly.
Be illustrated more clearly in letter in concrete technology contents of the present invention and the technology for making, below be illustrated again at significant advantage more of the present invention.
1, cooling of the present invention and cleaning merging method do not influence dye bath ratio, see accompanying drawing 1, in dyeing course, (1) route among the endless form of dye liquor such as the figure circulates, (2) among the cold water of heat exchanger 11 such as the figure, (3) route carry out, and therefore can not impact bath raio.
2, cooling of the present invention and cleaning merging method can contract the time of whole dyeing course, in the existing dyeing course, cooling has accounted for the most time, as adopt direct cooling and cleaning method for dyeing machine of the present invention, just can with the cooling with cleaning process entirely also, naturally shortened the time of process.
For example, when dying PET, reduce to 60 ℃ by 130 ℃ during cooling, rate of temperature fall is 2 ℃/min, then needs 35 minutes consuming time; During washing, washing twice, about 40 minutes consuming time, cooling and washing about 75 minutes consuming time altogether, if adopt method of the present invention, then cooling and washing 35 minutes consuming time altogether economized 40 minutes fully.
3, method of the present invention also can be saved cooling water, this is because adopt method of the present invention, to cool off with cleaning process and merge, just cleaning section water is in the past brought the cooling procedure use, therefore no longer need unnecessary cooling water, also be about to traditional cooling section water and saved fully.
4, the above-mentioned method of the present invention can improve dyeing quality, this be because cool but with cleaning process in, most dye liquor impurity has also emitted together, because what dye liquor impurity partly adhered to again when low temperature can't be discharged on the dyeing and weaving thing, if utilize indirect cooling method of the prior art, can't discharge these impurity at all, therefore utilize method of the present invention, in cooling and cleaning process, just emitted most dye liquor impurity, so can improve dyeing quality, reduce the specking flaw that causes because of dye liquor impurity.
But 5, method conserver power source of the present invention, shown in above-mentioned example, when dying PET, cooling and washing about 75 minutes consuming time altogether, if adopt method of the present invention, then cooling and washing 35 minutes consuming time altogether economized 45 minutes fully, that is to say the main pump running supply of electric power that has economized 45 minutes.
Dyeing machine of the present invention directly cooling has following advantage with the method for cleaning merging:
1, dyeing course does not influence bath raio;
2, shorten the time of dyeing course;
3, reduce the water consumption of cooling;
4, reduce energy consumption;
5, improve dyeing quality;
In sum, technology contents of the present invention and technological thought do not appear in the newspapers in the prior art, and method of the present invention is all having outstanding feature aspect the time that shortens dyeing course, using water wisely, energy savings and the raising dyeing quality, and in the production of reality, there is utilization to be worth, for this reason, earnestly ask early this case is authorized.

Claims (3)

1, a kind of direct cooling and cleaning method for dyeing machine, it is that the cooling of pressure dyeing machine or dyeing at normal pressure machine is merged the method for handling with cleaning, wherein High Temperature High Pressure refers to temperature more than 100 ℃, absolute pressure 1kg/cm 2More than, normal pressure refers to an atmospheric pressure, it is characterized in that above-mentioned direct cooling and cleaning method for dyeing machine is as follows:
When implementing cooling and cleaning merging process, in high temperature-pressure dyeing machine, if when hydraulic pressure is lower than dyeing machine in-cylinder pressure, this moment heat exchanger cold water inlet before need install a water pump or increase cold water inlet pressure additional; As implementing cooling in the dyeing at normal pressure machine and cleaning merging process is that process does not then need heating pump;
When implementing cooling and cleaning merging process, the course of cold water has (two), as described in Fig. 2,3, cooling water along (2) in the accompanying drawing 2,3, (4) route or (2), (5) route carries out, and the two all inserts dyeing machine from the arrival end of main pump;
When implementing cooling and cleaning merging process, the control mode of dyeing machine liquid level also has two kinds: as described in Figure, (6) and (7) position in the accompanying drawing is pressed in liquid level control;
2, in accordance with the method for claim 1, it is characterized in that the kind of the dyeing machine that described method is suitable for is not limited to L type dyeing machine, the dyeing machine of other types also can adopt this method, as figure cartridge type dyeing machine.
3, in accordance with the method for claim 1, it is characterized in that employed hardware partly as shown in Figure 1 in the described method, software partly then comprises microcomputer controller, when being used to control dyeing machine liquid level and enforcement cooling and cleaning merging process, and each electromagnetic valve of required control.
CN96112918A 1996-12-31 1996-12-31 Direct cooling and cleaning method for dyeing machine Pending CN1186882A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN96112918A CN1186882A (en) 1996-12-31 1996-12-31 Direct cooling and cleaning method for dyeing machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN96112918A CN1186882A (en) 1996-12-31 1996-12-31 Direct cooling and cleaning method for dyeing machine

Publications (1)

Publication Number Publication Date
CN1186882A true CN1186882A (en) 1998-07-08

Family

ID=5121662

Family Applications (1)

Application Number Title Priority Date Filing Date
CN96112918A Pending CN1186882A (en) 1996-12-31 1996-12-31 Direct cooling and cleaning method for dyeing machine

Country Status (1)

Country Link
CN (1) CN1186882A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102644171A (en) * 2012-04-18 2012-08-22 无锡市华洋染整机械有限公司 Cooling cloth washing system for dyeing machine under state of high temperature and high pressure
CN102912576A (en) * 2012-09-27 2013-02-06 周杰 Group-type waste heat absorbing and utilizing system
CN110662474A (en) * 2017-05-23 2020-01-07 美诺两合公司 Cleaning device and method for operating a cleaning device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102644171A (en) * 2012-04-18 2012-08-22 无锡市华洋染整机械有限公司 Cooling cloth washing system for dyeing machine under state of high temperature and high pressure
CN102912576A (en) * 2012-09-27 2013-02-06 周杰 Group-type waste heat absorbing and utilizing system
CN102912576B (en) * 2012-09-27 2015-05-13 周杰 Group-type waste heat absorbing and utilizing system
CN110662474A (en) * 2017-05-23 2020-01-07 美诺两合公司 Cleaning device and method for operating a cleaning device

Similar Documents

Publication Publication Date Title
CN111979679A (en) Energy-saving emission-reducing hot water control circulating system of dye vat
CA2066181A1 (en) Displacement heating in continuous digesters
CA2570997A1 (en) Methods to decrease scaling in digester systems
CN1186882A (en) Direct cooling and cleaning method for dyeing machine
CN1022499C (en) Method and apparatus to displace digester from both end
CN214371843U (en) Energy-saving circulating water system
CN210314867U (en) Energy-saving emission-reducing hot water control circulating system of dye vat
CN109925748A (en) It is a kind of that the liquid degassing device and method of removing gas liquid can be automatically continuously provided
CN1057579C (en) Method for directly cooling and washing dyeing machine
AU2008307020B2 (en) A method and an apparatus for directly heating slurry
CN212103321U (en) Dyeing washing device
JPH01148889A (en) Method and apparatus for reducing formation of scale in pulp producing operation
CN113584275A (en) Online quenching water temperature control and circulation system for aluminum profile
CN220530935U (en) Promote high-efficient driving system of leaf filter operation
CN210561233U (en) Cooling water washing water delivery device for high-temperature direct-discharging water washing machine
CN116870575A (en) Efficient driving method and system for improving operation of leaf filter
CN1358897A (en) Method for dye by connected dye vats
CA1242552A (en) Method of bringing a digester up to cooking temperature
CN201007472Y (en) Circulating water heat energy reuse device of firepower plant
CN218755600U (en) Energy-saving coal tar processing system
CN215195440U (en) Evaporator
CN218210975U (en) Water cooling system cleaning device without stopping
CN218579889U (en) Sump oil recovery processing system
CN219995320U (en) Energy-saving and water-saving system based on starting and stopping working conditions of large thermal power plant unit
CN203513532U (en) Crude glycerol refining technology system

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C01 Deemed withdrawal of patent application (patent law 1993)
WD01 Invention patent application deemed withdrawn after publication