Multi-pipe quantitative medium filling system of supercritical fluid dyeing machine
10294598 ยท 2019-05-21
Assignee
- NANTONG TEXTILE & SILK INDUSTRIAL TECHNOLOGY RESEARCH INSTITUTE (Nantong, CN)
- SOOCHOW UNIVERSITY (Suzhou, CN)
Inventors
Cpc classification
D06B23/205
TEXTILES; PAPER
D06B19/00
TEXTILES; PAPER
D06B23/20
TEXTILES; PAPER
International classification
D06P1/94
TEXTILES; PAPER
D06B23/20
TEXTILES; PAPER
Abstract
The invention relates to a multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine. The system comprises a supercritical fluid medium reservoir, a stop valve, and a medium filter sequentially connected by a high-pressure main pipe, and at least two filling branches independent of each other and connected to the medium filter. Each filling branch includes a booster pump, a supercritical fluid high-pressure mass flowmeter, a ball valve, and a dyeing unit sequentially connected along a medium forward direction by a high-pressure branch pipe. By using a mass-measurement filling system having multiple branches independent of each other, the invention can effectively realize simultaneous and accurate quantitative medium filling for separate dyeing units and differentiated filling for dyeing units with different medium masses, thus overcoming disadvantages such as unreliability, inaccuracy and low use efficiency of a conventional method, and also making a dyeing operation simple and scientifically feasible.
Claims
1. A multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine, comprising: a supercritical fluid medium reservoir, a stop valve, and a medium filter sequentially connected by a high-pressure main pipe; and at least two filling branches independent of each other and connected to the medium filter, and each of the filling branches comprising a booster pump, a supercritical fluid high-pressure mass flowmeter, a high-pressure ball valve and a dyeing unit which are sequentially connected along a medium forward direction by a high-pressure branch pipe, wherein the supercritical fluid medium reservoir is provided with a medium inlet connected to a gas source, and a medium outlet connected to the stop valve by the high-pressure main pipe; an entry end of the booster pump being in communication with the high-pressure main pipe to be connected with the medium filter, an exit end of the booster pump being in communication with the supercritical fluid high-pressure mass flowmeter, and the start and stop of the booster pump being controlled by the supercritical fluid high-pressure mass flowmeter; an entry end of the supercritical fluid high-pressure mass flowmeter being in communication with the booster pump by the high-pressure branch pipe, an exit end of the supercritical fluid high-pressure mass flowmeter being in communication with the high-pressure ball valve by the high-pressure branch pipe, and the supercritical fluid high-pressure mass flowmeter being connected to the booster pump in a coordinated control manner, and the start and stop of the booster pump being controlled by coordinated control signals for measurement and transmission of the mass, density and temperature of a passing supercritical fluid, and presetting of a required fluid mass; and one end of the high-pressure ball valve being in communication with the supercritical fluid high-pressure mass flowmeter by the high-pressure branch pipe, and the other end of the high-pressure ball valve being connected to the dyeing unit for quantitatively filling the dyeing media.
2. The multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine as claimed in claim 1, wherein the gas source passes through a high-pressure pipe and a stop valve, and enters the supercritical fluid medium reservoir after being treated by a condenser.
3. The multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine as claimed in claim 2, wherein the dyeing units are further connected with a separation and recycling device by the high-pressure main pipe, and the separation and recycling device being connected with the condenser by means of a stop valve.
4. The multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine as claimed in claim 3, wherein the stop valve for introducing the gas source and the stop valve connected with the separation and recycling device are connected with the condenser by a high-pressure three-way pipe.
5. The multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine as claimed in claim 4, wherein the dyeing unit is a stationary high-pressure dye vat or a mobile high-pressure treatment container.
6. The multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine as claimed in claim 1, wherein the medium inlet is provided at a distance of 10 to 50 cm from the top of the supercritical fluid medium reservoir, and the medium outlet is provided at a distance of 5 to 50 cm from the bottom of the supercritical fluid medium reservoir.
7. The multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine as claimed in claim 1, wherein the supercritical fluid high-pressure mass flowmeter has an applicable pressure of 0 to 70 MPa and a applicable temperature of 50 C. to 150 C.
8. The multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine as claimed in claim 1, wherein the booster pump is selected from a group consisting of a gas booster pump, a liquid booster pump, a high-pressure plunger pump and a diaphragm pump.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2) In the drawings, 1. supercritical fluid medium reservoir; 1-1. medium outlet; 1-2 medium inlet; (2, 9, 10, 12, 13) stop valve; 3. medium filter; 4. booster pump; 5. supercritical fluid high-pressure mass flowmeter; 5-1 coordinated control signal of the mass flowmeter and the booster pump; 6. ball valve; 7. dyeing unit; 8. separation and recycling device; 10-1. high-pressure three-way pipe; 11. condenser; 14. high-pressure main pipe; (n.sub.1, n.sub.2, . . . , n.sub.i-1, n.sub.i, i2). filling branches.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
(3) The invention will be further illustrated in more detail with reference to the accompanying drawings and embodiments. It is noted that, the following embodiments only are intended for purposes of illustration, but are not intended to limit the scope of the present invention.
(4) Referring to
(5) The filling branches n.sub.1, n.sub.2, . . . , n.sub.i-1, n.sub.i (i2) independent of each other are in communication with the high-pressure main pipe 14 sequentially. In each filling branch, the booster pump 4, the supercritical fluid high-pressure mass flowmeter 5, the high-pressure ball valve 6, and the dyeing unit 7 are sequentially connected by a high-pressure branch pipe along the medium forward direction. The entry end of each of the booster pumps 4 is in communication with the high-pressure main pipe 14, and the exit end of each of the booster pumps 4 is connected to the supercritical fluid high-pressure mass flowmeters 5. In addition, the exit end of the supercritical fluid high-pressure mass flowmeter 5 is in communication with the high-pressure ball valve 6 by the high-pressure branch pipe, and the high-pressure ball valve 6 is connected to the dyeing unit 7 by the high-pressure branch pipe. The supercritical fluid high-pressure mass flowmeter 5 can directly implement the measurement and display of the mass, density, and temperature of the supercritical fluid flowing through the branch where the supercritical fluid high-pressure mass flowmeter 5 is located, and can preset a required fluid mass, thereby realizing coordinated control over the start/stop and flow of the booster pump 4 by using a coordinated control signal 5-1 of the supercritical fluid high-pressure mass flowmeter 5 and the booster pump 4, to achieve quantitative mass filling of the supercritical fluid medium in each separate dyeing unit 7.
(6) The medium filter 3 on the high-pressure main pipe 14 is connected to the medium outlet 1-1 of the supercritical fluid medium reservoir 1. The medium filter 3 can achieve and ensure purification treatment for the medium to be filled.
(7) Under the coordinated control of the corresponding supercritical fluid high-pressure mass flowmeters 5 and the booster pumps 4, the filling branches n.sub.1, n.sub.2, . . . , n.sub.i-1, n.sub.i (i2) independent of each other can realize simultaneous and accurate quantitative medium filling for multiple independent dyeing units 7 and differentiated filling of different medium masses for different dyeing units 7.
(8) A medium gas source required by the system of the present invention is connected into the system by a high-pressure three-way pipe 10-1 and a stop valve 10, and after being treated by a condenser 11, the gas source enters the supercritical fluid medium reservoir 1 for later use.
(9) In each branch, by the high-pressure branch pipe, one end of the high-pressure ball valve 6 is in communication with the dyeing unit 7, and the other end is in communication with the supercritical fluid high-pressure mass flowmeter 5. By opening the high-pressure ball valve 6, the supercritical fluid medium reservoir 1 is in communication with the dyeing unit 7, to quantitatively fill the dyeing unit 7 with the required dyeing medium.
(10) In each branch, the booster pump 4 may be a gas booster pump, a liquid booster pump, a high-pressure plunger pump or a diaphragm pump. The outlet of the booster pump 4 is in communication with the supercritical fluid high-pressure mass flowmeter 5 by the high-pressure branch pipe. The start/stop and flow of the booster pump 4 are controlled by an output signal from the downstream supercritical fluid high-pressure mass flowmeter 5, to realize quantitative filling for the dyeing unit 7.
(11) The supercritical fluid medium reservoir 1 is provided with a medium outlet 1-1 and a medium inlet 1-2. The medium outlet 1-1 is disposed at a distance of 5 to 50 cm from the bottom of the supercritical fluid medium reservoir 1, and is connected to the stop valve 2 by the high-pressure main pipe 14, and the stop valve 2 is further connected to the medium filter 3. The medium inlet 1-2 is disposed at a distance of 10 to 50 cm from the top of the supercritical fluid medium reservoir 1, and is connected to a stop valve 12 and the condenser 11 successively by the high-pressure main pipe, to achieve the functions such as receipt, storage, and output of the medium gas source.
(12) The dyeing units 7 independent of each other may be various stationary high-pressure dye vats of different forms, different shapes, and different volumes, or may be mobile high-pressure treatment containers for textile dyeing, pre-treatment or after-treatment. One end of the dyeing unit 7 is connected to the high-pressure ball valve 6, and the other end may be or not be connected to a separation and recycling device 8, a stop valve 9, and the condenser 11 successively as required.
(13) When the multi-pipe quantitative medium filling system of a supercritical fluid waterless dyeing machine according to the present invention operates, first, the stop valves 9, 13 and 2 are closed, and the stop valves 10 and 12 and the condenser 11 are opened. The medium gas source is used for filling the storage medium for the supercritical fluid medium reservoir 1 by the high-pressure three-way pipe 10-1. After the filling is finished, the stop valve 10 is closed, and the gas source is cut off. The dyeing units 7 to be filled are connected into the filling branches n.sub.1, n.sub.2, . . . , n.sub.i-1, n.sub.i (i2) by the high-pressure branch pipes respectively, and are connected to the high-pressure ball valves 6 in the branches respectively. Also, medium masses required for dyeing are preset by means of the corresponding supercritical fluid high-pressure mass flowmeters 5 respectively. Then, the stop valve 2 in the high-pressure main pipe 14 is opened, and the high-pressure ball valves 6 in the branches are opened, to start the supercritical fluid high-pressure mass flowmeters 5 in the branches to quantitatively fill the dyeing units 7 with the dyeing medium. In addition, the supercritical fluid high-pressure mass flowmeter 5 in each branch monitors and displays the temperature, density, transient flow and accumulated flow of the medium flowing through the branch, and transmits the mass information of the medium to be filled to the corresponding booster pump 4 by the coordinated control signal 5-1, to realize coordinated control over the start/stop and flow of the booster pump 4, thereby achieving the one-time, accurate and quantitative filling of the required supercritical fluid medium for each corresponding dyeing unit 7. When the predetermined filling mass of the medium is reached in a dyeing unit 7, the corresponding booster pump 4 is automatically stopped, and then the high-pressure ball valve 6 in the branch is closed, and thus the quantitative filling for the dyeing unit 7 is accomplished.
(14) For the stationary dyeing unit, after the filling is finished, the temperature of each dyeing unit may be increased directly according to a predetermined dyeing process, to complete the dyeing procedure. For the mobile dyeing unit, the dyeing unit may be disconnected from the filling branch, and then moved into an appropriate device for heating and dyeing. Furthermore, for each filling branch, the foregoing procedure may be repeated to continue quantitative filling for other dyeing units to be filled, to realize the efficient utilization of the filling and boosting system.
(15) Furthermore, a stationary dyeing unit or a mobile dyeing unit, may be connected to the separation and recycling device 8 as required after the dyeing is finished, to accomplish separation and recycling of the dyeing medium and residual dye, and treatment of products after dyeing, and so on.
(16) The above description is only preferred embodiments of the present invention and not intended to limit the present invention, it should be noted that those of ordinary skill in the art can further make various modifications and variations without departing from the technical principles of the present invention, and these modifications and variations also should be considered to be within the scope of protection of the present invention.