Apparatus for batch dyeing

Information

  • Patent Grant
  • 6672114
  • Patent Number
    6,672,114
  • Date Filed
    Thursday, January 10, 2002
    22 years ago
  • Date Issued
    Tuesday, January 6, 2004
    20 years ago
Abstract
The jet dye apparatus includes a reactant chamber for the processing or various materials and liquids, and a pump for recirculating the liquids to and from the reactant chamber. A jet venturi or nozzle receives the material from the reactant chamber and returns the material to the reactant chamber through a return tube. A portion of the liquids from the pump are supplied to the jet venturi. An inductor receives a portion of the liquids from the pump before they are returned to the reactant chamber. The inductor combines the liquids with granular or powder additives from an additive container.
Description




BACKGROUND




The present invention generally relates to apparatuses for the process of dyeing and treating material, and in particular, to apparatuses for the batch process of dyeing material.




In a batch dyeing process, a material is subjected to various conditions in order to accomplish the dyeing of the material. In one of these conditions, the material is scoured after the dyeing substances are applied in an effort to remove any residual dyeing substances on the material. The chemicals that are used for scouring can be very volatile and reactive chemicals. In particular, reductive powders or the granular form of the scouring chemicals are highly volatile.




The scouring chemicals must only be added to the batch process at a specific critical time in the dyeing process. Additionally, the scouring chemicals must be blended into the liquids of the batch dyeing process in a manner that reduces the possibility of the reactive scouring chemicals contacting the material in a concentrated form or consistent method. For these reasons, scouring chemicals are typically added to the batch dyeing process in a liquid form.




However, additive liquid scouring materials often exhibit different characteristics than the granular or powder scouring chemicals. Additionally, many of the powder or granular scouring chemicals begin to degredate immediately upon combination with an additive liquid before addition to the liquids in a batch dye process.




Therefore, there is a need for apparatuses that can add powder or granular additives, such as scouring chemicals, to a batch process for treating a material, such as a batch dyeing process, in a controlled manner.











BRIEF DESCRIPTION OF THE DRAWINGS




The present invention can be better understood with reference to the following figures:





FIG. 1

is a diagram illustrating a jet dyeing apparatus of the prior art.





FIG. 2

is a diagram illustrating a jet dyeing apparatus with the improvements of the present invention thereon.





FIG. 3

is a cross sectional view of the eductor and holding device from the improvement of the present invention illustrated in FIG.


2


.











DETAILED DESCRIPTION




The present invention generally relates to the addition of granular or powder additives into a batch dye process, such as a dye process using a prior art jet dye apparatus


100


as illustrated in FIG.


1


. The jet dye apparatus


100


generally includes a reactant or kier chamber


111


for the processing of various materials, such an loop of textile


10


, with various liquid dyes and chemicals


20


. As illustrated, the textile


10


progresses from the reactant chamber


111


over a lifter reel


112


which is rotated by a motor


113


. After passing over the lifter reel


112


, the textile


10


passes through a jet nozzle or venturi


114


which exhausts into a return tube


115


. The return tube


115


empties the materials into the opposite end of the reactant chamber


111


from the jet venturi


114


.




The liquids


20


are removed from the bottom of the reactant chamber


112


through drain or suction ports


121




a


and


121




b


in the bottom of the reactant chamber


111


. The liquids


20


from the suction ports


121




a


,


121




b


, pass through recirculated flow control values


122




a


and


122




b


to the pump


123


. The pump


123


forces the liquids


20


through a filter


124


and a heat exchanger


125


. The liquids


20


leave the heat exchanger


125


and are forced through a venturi pressure control valve


126


into the jet venturi


114


, and to a spray assembly


127


located in the top of the reactant chamber


111


. To remove liquids


20


from the batch system in the jet dye apparatus


100


, a system drain valve


128


is positioned before the pump


123


, which allows the draining of the liquids


20


from the system.




At various times during the batch process, it will be necessary to add dye solutions and/or chemical solutions to the liquids


20


in the batch process. The liquids


20


under pressure from the pump


123


are received in a supply recirculation passage


131


after passing through the heat exchanger


125


. The liquids


20


from the supply recirculation passage


131


pass through recirculation flow control valves


132




a


and


132




b


before reaching supply recirculation eductors


133




a


and


133




b


, respectively. The liquid dye supply or liquid chemical supply are provided to suction side of the supply recirculation eductors


133




a


or


133




b


, respectively, after passing through supply control valves


134




a


or


134




b


, respectively. The combination of recirculation liquids and the additive fluids from the supply recirculation eductors


133




a


,


133




b


, are returned to the stream of liquid coming from the suction ports


121




a


,


121




b


, prior to the recycled control valves


122




a


or


122




b


. Supply recirculation check valves


135




a


and


135




b


prevent fluids from back flowing into the supply recirculation eductors


133




a


and


133




b


, respectively, from the drain ports


121




a


or


121




b.






Referring now to

FIG. 2

, there shown the improvement of the present invention as illustrated on the batch jet dye apparatus


100


. The batch jet dye apparatus operates as described above with respect to

FIG. 1

, with the improvements of the present invention. The improvements of the present invention generally comprise the addition of an additive recirculation circuit


210


, an additive eductor


220


, an additive supply apparatus


230


, and an extinguishing system


240


. As used herein, the term eductor shall mean a device that uses the flow of a fluid to mix another substance with that fluid.




The additive recirculation circuit


210


includes an additive recirculation receipt passage


211


, additive recirculation flow control valves


212


and


213


, an additive recirculation supply passage


214


, and an additive recirculation check valve


215


. The additive recirculation receipt passage


211


receives liquid


20


under pressure by the pump


123


after the heat exchanger


125


, and provides that liquid


20


via the first additive recirculation control valve


212


to the additive eductor


220


. The additive eductor


220


adds and mixes a granular or powder additive


30


from the additive supply apparatus


230


into the liquid


20


throttling through the additive eductor


220


. The liquid


20


leaving the additive eductor


220


passes through the second additive recirculation control valve


213


and is provided by the additive recirculation supply passage


214


to the stream of liquid from the suction port


121




a


to the recycled control valve


122




a


, via the additive recirculation check valve


215


. In this manner, the additive recirculation check valve


215


prevents fluid from the drain port


121




a


from entering the additive recirculation supply passage


214


. In another embodiment, the additive recirculation supply passage


214


returns the liquid


20


from the additive eductor


220


to the reactant chamber


111


, via the additive recirculation check valve


215


, below a false bottom in the reactant chamber


111


that holds the material


10


from the discharge of the liquid


20


from the additive recirculation supply passage


214


and the suction ports


121




a


and


121




b.






Referring now to

FIG. 3

, there is shown a cross sectional view of the additive eductor


220


, the additive supply apparatus


230


, and the extinguishing system


240


. The additive eductor


220


, as illustrated in

FIG. 3

, is a jet pump. An example of a jet pump that can be used in the present invention is the model LM Jet Pump by Penberthy, Inc., in Prophetston, Ill. As illustrated in

FIG. 3

, the eductor


220


generally includes an inlet section


221


, a suction section


223


, and a discharge section


224


. The inlet section


221


receives the liquid


20


from the additive recirculation receipt passage


211


, and passes that liquid through an inlet nozzle


221


which directs the liquid


20


through the suction chamber


223


into the discharge section


224


. The smaller diameter of the inlet nozzle


222


accelerates the liquid


20


as it passes through the suction chamber


223


, thereby inducing substances in the suction chamber


223


to entrain with the liquid


20


passing into the discharge section


224


. The discharge section


224


includes a parallel section


225


, and a diffuser section


226


. The substance from the suction chamber


223


entrained in the liquid


20


mixes with the liquid


20


and acquires energy in the parallel section


225


of the discharge section


224


. As the liquid


20


passes through the diffuser


226


of the discharged section, the mixture is converted to a pressure greater than the section pressure.




The additive supply apparatus


230


generally comprises a additive supply valve


231


that provides the dry additive


30


from an additive container or holding device


232


to the additive passage


226


in the additive eductor


220


. As illustrated, the additive supply valve


231


is a butterfly type valve that can be controlled by the controls operating the system. Side walls


232




a


of the holding device


232


are preferably sloped to avoid bridging of the powder or granular additive


30


, which would inhibit the flow of the additive


30


from the holding device


232


to the additive eductor


220


. The side walls


232




a


slope to the additive supply valve


231


, thus preventing horizontal surfaces in the additive holding device


232


which can hold some of the additive


30


from passing into the additive eductor


220


. In one embodiment, the side walls


232




a


of the holding device


232


are angled not more than about 45 degrees from the vertical. In another embodiment, the side walls


232




a


of the holding device


232


are angled not less than about 25 degrees from the vertical.




A lid


233


is secured to the holding device


232


by an hinge


234


for protecting the additive


30


inside the holding device


232


. The lid


233


also includes a hinge shield


235


for protecting the hinge


234


from the additive


30


, and the additive


30


from any material that my incidentally pass through or from the hinge


234


. A lid locking mechanisum, such as the lid lock solenoid


236


, inhibits the opening of the lid


234


until a lid lock control


237


releases the lid lock solenoid


236


. The lid lock control


237


can be an activation providing the current necessary to activate the solenoid


236


upon pushing a button or throwing a switch, or a part of the process control for the batch system that only activates the solenoid


236


during critical times of the process, including before and/or after the process. In the event that the additive is also corrosive or reacting some, or all, of the holding device side walls


232




a


, lid


233


, hinge


234


, hinge shield


235


, additive supply valve


231


, and/or eductor


220


can be formed of 316 stainless steel.




A holding device vibrator


238


attached to the hopper


232


facilities the progression of the dry additive


20


through the hopper


232


. A regulator


239


controls the operation of the hopper vibrator


238


. Use of the holding device vibrator


238


helps prevent bridging of the additive


30


in the holding device


232


, and helps reduce the possibility of small amounts of the additive


30


to cling to the side walls


232




a


of the additive holding device


232


and not pass into the additive eductor


220


. Additionally, providing the insides or face of the side walls


232




a


with a mirror type surface will facilitate the progression of the additive


30


to the eductor


220


.




The extinguishing system


240


can be a supply inlet


242


into the holding device


232


that is controlled by a mechanism such as a valve


244


. The extinguishing medium that is supplied by the extinguishing system


240


must be selected appropriately to accommodate the additive in the holding device


232


. When the appropriate extinguishing medium is water, the extinguishing system


240


can also be used to clean the holding device


232


. The extinguishing system


240


can also be used to place a gas pad or protective gas layer on the additive


30


in the additive holding device


232


.




In a batch dyeing process, the granular or powder scouring chemicals are placed in the additive holding device


232


just prior to the need for the chemicals. The locking mechanism


236


can be used to prevent adding the chemicals to the holding device


232


until close to the critical time the chemicals are needed, in order to reduce any risks associated with having the chemicals out of a controlled environment. Once the additive chemicals


30


are placed in the holding device


232


, a gas layer can be placed on the additive


30


, such as nitrogen, to give added protection to the chemicals


30


in the holding device


232


. Once the batch process is at the point where the granular or powder additives are needed, the flow control valves


212


and


213


are opened to create a flow of liquid


20


through the additive eductor


220


, and then the additive supply valve


231


opens to allow the additive


30


to be drawn into and mix with the liquid


20


within the additive eductor


220


. After the appropriate amount of additive


30


has be mixed into the liquid


20


, the additive supply valve


231


is closed and then the flow control valves


212


and


213


are closed. The control of components of the additive recirculation circuit


210


, the additive eductor


220


, the additive supply apparatus


230


, and the extinguishing system


240


, can be controlled by a processor, such as the processors used on many of the prior art jet dye apparatuses to control the various components of that system.




Although the present invention has be described herein by reference to specific examples, the present invention is not mean to be limited by the specific details of those descriptions. For example, the additive eductor can be connected such that liquid flowing through the eductor is taken from the flow of liquid that has left the pump and returned as all, or some, of the liquid that is returned into the reactant chamber via the jet, sprays, or another inlet. As another example, the additive eductor can be connected such that the liquid flowing through the additive eductor is taken from the fluid leaving the reactant chamber, such as from the drain ports or another outlet, and returned as all, or some of the liquid flowing to the pump. In each of these examples, the additive eductor, the check valves, and the control valves will require orientation to accommodate the flow direction of the batch process. Additionally, flow restrictions may be necessary in any liquid flow parallel to the liquid flowing through the additive eductor, in order to maintain the liquid flow through the additive eductor.



Claims
  • 1. An apparatus for mixing an additive with a liquid, and batch processing of a material with the liquid containing the additive, the apparatus comprising:a reactant chamber, the reactant chamber providing a space for the processing of the material with the liquid containing the additive; a pump connected to receive the liquid from the reactant chamber and to return the liquid to the reactant chamber; a jet connected to receive the material from the reactant chamber, the jet further being connected to receive at least a portion of the liquid from the pump, before the liquid reaches the reactant chamber; a return tube for returning the material and the liquid from the jet to the reactant chamber; an additive container for holding the additive in a powder or granular form, the additive container having an additive output opening for the exit of the additive in the powder or granular form from the additive container, the additive container further having side walls angled relative to the vertical of the additive container such that the additive in the powder or granular form is directed towards the additive container output; and, an eductor connected between the pump and the reactant chamber such that at least a portion of the liquid passing through the pump and returning to the reactant chamber also flows through the eductor, the eductor further being connected to the additive container output such that the additive from the additive container is mixed with the liquid flowing through the eductor.
  • 2. The apparatus according to claim 1, wherein the eductor is connected such that the flow of the liquid through the eductor is taken from the liquid flowing from the pump and returned to the liquid flowing to the pump.
  • 3. The apparatus according to claim 2, further including a gas supply system connected to the additive container for dispensing a protective gas layer over the additive.
  • 4. The apparatus according to claim 1, wherein the eductor is connected such that the flow of the liquid through the eductor is take from the liquid flowing from the pump and returned to the reactant chamber.
  • 5. The apparatus according to claim 1 further including the lifter wheel inside the reactant chamber, the lifter wheel being positioned for the material to pass over the lifter wheel just prior to entering the jet.
  • 6. The apparatus according to claim 5, further including the lifter wheel being motorized.
  • 7. The apparatus according to claim 1, further including a heat exchanger connected to exchange heat with at least a portion of the liquid flowing through the pump.
  • 8. The apparatus according to claim 1, further including spray nozzles located in an upper portion of the reaction chamber, and wherein a portion of the liquid from the pump returning to the reactant chamber passes through the spray nozzles.
  • 9. The apparatus according to claim 1, wherein the side walls of the additive container are angled no more than about 45 degrees from the vertical.
  • 10. The apparatus according to claim 1, wherein the side walls of the additive container are angled no less than about 25 degrees from the vertical.
  • 11. The apparatus according to claim 1, wherein the additive container includes a valve positioned to control the flow of the additive from the additive container output to the eductor.
  • 12. The apparatus according to claim 11, wherein the valve comprises a butterfly valve.
  • 13. The apparatus according to claim 1, wherein the additive container includes a lid.
  • 14. The apparatus according to claim 13, wherein the additive container further includes a lid locking mechanisum.
  • 15. The apparatus according to claim 14, wherein the lid locking mechanisum comprises a solenoid.
  • 16. The apparatus according to claim 1, further including a vibrator mounted to the additive container such that the vibrator will apply vibration to the side walls of the additive container.
  • 17. The apparatus according to claim 1, further including a check valve connected after the eductor such that liquid flow towards the eductor is inhibited.
  • 18. The apparatus according to claim 1, further including a valve positioned before the eductor to control the flow of the liquid to the eductor.
  • 19. The apparatus according to claim 1, further including a valve positioned after the eductor to control the flow of the liquid from the eductor.
  • 20. The apparatus according to claim 1, further including an extinguishing system connected to the additive container for dispensing an extinguishing medium to the additive.
US Referenced Citations (15)
Number Name Date Kind
3510251 Fujii et al. May 1970 A
3587256 Spara Jun 1971 A
3685325 Carpenter Aug 1972 A
3780544 Turner et al. Dec 1973 A
3921420 Aurich et al. Nov 1975 A
3949575 Turner et al. Apr 1976 A
4483032 Christ et al. Nov 1984 A
4656846 Damm Apr 1987 A
4716744 Turner et al. Jan 1988 A
4829620 Christ et al. May 1989 A
4873847 Kasai et al. Oct 1989 A
4881384 Chicharro Nov 1989 A
5170523 Scholl Dec 1992 A
5520027 McCartney et al. May 1996 A
5850651 Ishimaru et al. Dec 1998 A
Non-Patent Literature Citations (2)
Entry
Tri-Clover, Inc.; Tri-Blender sets the pace with fast and uniform In-Line or Batch Blending; 1989.
Penberthy. Inc.; Section 1000, Bulletin 1200, Penberthy—Jet Pump Technical Data—Pumping Liquids; 5/87.