Method for pickling steel sheets

Abstract

The invention relates to a method for pickling steel sheets 8, the steel sheets being continuously dipped in a pickling bath 1, containing a pickling solution 10, the bath being connected to a treatment unit including a recirculation tank 3, circulators 12 and 13, a continuous entering flow 11 of the solution being fed into an ultrafiltration device 2 from the recirculation tank 3 and two flows exiting the ultrafiltration device, one filtered exiting flow 21 being then fed back inside the recirculation tank 3 and one unfiltered flow 22, the treatment unit including no storage tank.

Claims

1. A method for pickling steel sheets, the method comprising: continuously dipping steel sheets in a pickling bath containing a pickling solution, the pickling bath being connected to a treatment unit including a recirculation tank, at least one circulator, a continuous entering flow of the pickling solution being fed into an ultrafiltration device from the recirculation tank and two flows exiting the ultrafiltration device, the two flows including one filtered exiting flow fed back into said recirculation tank and one unfiltered flow, the treatment unit including no storage tank.

2. The method as recited in claim 1 wherein the pickling solution is made of one or a combination of different acids.

3. The method as recited in claim 1 wherein the pickling solution is not treated thermically before being fed into the ultrafiltration device.

4. The method as recited in claim 1 wherein neither an additive nor a device is used to increase a degree of polymerization of the pickling solution fed into the ultrafiltration device.

5. The method as recited in claim 1 wherein the ultrafiltration device is a cross-flow ultrafiltration device.

6. The method as recited in claim 1 wherein the ultrafiltration device has at least one membrane.

7. The method as recited in claim 6 wherein the membrane is made of ceramic.

8. The method as recited in claim 6 wherein the membrane has a pore size comprised between 1 and 10 nm.

9. The method as recited in claim 1 wherein the continuous entering flow of the pickling solution is fed into the ultrafiltration device at a flow rate between 5 and 50 m.sup.3.Math.h.sup.1, so as to allow renewal of an acid volume in the recirculation tank of between 1 and 10 times per hour.

10. The method as recited in claim 1 wherein the filtered exiting flow is between 50 and 95% of the continuous entering flow of the pickling solution being fed into the ultrafiltration device.

11. The method as recited in claim 1 wherein the continuous entering flow has a silicon content of at least 60 mg.Math.L.sup.1.

12. The method as recited in claim 1 wherein the ultrafiltration device includes several cross-flow ultrafiltration devices.

13. The method as recited in claim 1 further comprising backwashing the ultrafiltration system to clean the membrane.

14. The method as recited in claim 1 wherein the unfiltered flow is concentrated in silicon, and further comprising treating the unfiltered flow exiting the ultrafiltration system.

15. An equipment comprising: a pickling bath; a transporter continuously dipping steel sheets in the pickling bath; a treatment unit including a recirculation tank having an inlet and an outlet connected to the pickling bath, a further outlet of the recirculation tank connected to an inlet of an ultrafiltration device, a first outlet of the ultrafiltration device connected to a further inlet of the recirculation tank and a second outlet of the ultrafiltration device being provided for an unfiltered flow, the treatment unit including no storage tank.

16. The equipment as recited in claim 15 wherein the second outlet is connected to a wastewater treatment.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) To illustrate the invention, various embodiments and trials of non-limiting examples will be described, particularly with reference to the following figure:

(2) FIG. 1 is a schematic illustration of the installation.

DETAILED DESCRIPTION

(3) The invention relates to a method for pickling steel sheets 8, said steel sheets being continuously dipped in a pickling bath 1, containing a pickling solution 10, said bath being connected to a treatment unit including a recirculation tank 3, circulation means 12 and 13, a continuous entering flow 11 of said solution being fed into an ultrafiltration device 2 from the recirculation tank 3 and two flows exiting the ultrafiltration device, one filtered exiting flow 21 being then fed back into said recirculation tank 3 and one unfiltered flow 22, said treatment unit including no storage tank.

(4) In the prior art, the clogging of the recirculation system is not dealt with. With the method according to the present invention, it seems that the clogging is slowed down which apparently prolonged the lifetime of recirculating system, i.e. pumps, nozzles, pipes and valves.

(5) Moreover, compared to the closest prior art, the pickling method according to the present method does not use a storage tank. This enables the present method to minimize the polymerization kinetics rate of colloidal silicon leading to a decrease of the fouling tendency of the membrane.

(6) Preferably, said pickling solution 10 is made of one or a combination of different acids. For example, hydrochloric acid at 15% is in the pickling bath 1 or a mix of hydrochloric acid and sulphuric acid.

(7) Preferably, said pickling solution 10 is not treated thermically before being fed into said ultrafiltration device. It seems that it permits to immediately treat the pickling acid and also requires less space.

(8) Preferably, neither additive, nor device is used to increase the degree of polymerization of said solution being fed into said ultrafiltration device. However, in the previous patents, the acidic pickling wastewater is settled in a tank increasing the degree of polymerization and thus permitting to obtain bigger particles. This settling process presented in the previous patent seems to ease the filtration due to a global increase of the particle size to be filtered. Consequently, the removal rate achieved is above 99% in the case of the patent WO 2014/36575 and 75% for AT 411 575. On the contrary, the present invention has apparently the major advantage of drastically slowing down the clogging with a removal rate of only 40% of the total silicon content in the used pickling acid solution. So the objective is achieved but the space required is reduced.

(9) Preferably, the ultrafiltration device 2 is a cross-flow ultrafiltration device. In the case of a cross-flow filtration, it is believed that contrary to a dead-end filtration, the flow is applied tangentially across the membrane surface. Without willing to be bound by any theory, as feed flows across the membrane, the filtrate passes through the holes of the membrane while the unfiltered flow exits at the opposite end of the membrane. Apparently, the tangential flow of the membrane creates a shearing effect on the surface of the membrane, which in turn reduces fouling.

(10) Preferably, the used acid pickling is circulated using pumps. The pumps are protected by a cartridge filter permitting filtering of the suspended solids.

(11) Preferably, the ultrafiltration device 2 has one or several membranes. Preferably, the membrane of the ultrafiltration device 2 is made of ceramic.

(12) Preferably, the membrane of the ultrafiltration device 2 has a pore size comprised between 1 and 10 nm. For example, the membrane has a pore size of 7 nm.

(13) Preferably, the continuous flow has a silicon content of at least 60 mg.Math.L.sup.1, more preferably of 100 mg.Math.L.sup.1 and even more preferably of 150 mg.Math.L.sup.1. Apparently, the present invention has also the advantageous effect of being more efficient with higher silicon concentration because more colloidal silicon is present and thus facilitates the filtration. Without willing to be bound by any theory, this technology assures a rejection rate of 100% of colloidal and suspended matter bigger than the membrane pore size.

(14) Preferably, the continuous flow 11 of said solution is fed into the ultrafiltration device at a flow rate comprised between 5 and 50 m.sup.3.Math.h.sup.1, preferably between 15 and 30 m.sup.3.Math.h.sup.1, permitting to renew between 1 and 10 times per hour the acid volume present in recirculation tank, preferably 4 times per hour.

(15) Preferably, the purified exiting flow is comprised between 50 and 95%, more preferably between 65 and 85%, of the flow of said solution being fed into an ultrafiltration device.

(16) Preferably, the ultrafiltration system is backwashed to clean the membrane. For example, the ultrafiltration system is backwashed every 8 minutes by a flow of tap water 24 and the tap water flow used to clean the membrane 23 exits said ultrafiltration device.

(17) It is also possible that the ultrafiltration device is composed of several cross-flow ultrafiltration devices. For example, the ultrafiltration device is composed of two cross-flow ultrafiltration devices.

(18) Preferably, the unfiltered flow, i.e. concentrated in silicon, exiting the ultrafiltration system (2) is treated. Preferably, this treatment can be done in a decanter or a hydrocyclone. After this treatment, the purified flow, i.e. having the lowest silicon concentration, can be fed back to the recirculation tank 3 or the ultrafiltration device 2. Preferably, the flow having the highest silicon concentration exiting the treatment device can be sent to an acid regeneration plant or to wastewater treatment 4.

(19) The invention also relates to an equipment comprising a pickling bath 1, a system continuously dipping steel sheets in said pickling bath and a treatment unit including a recirculation tank 3, at least an ultrafiltration device 2, pipes connecting said recirculation tank and tap water input 24 and backwashing solution output 23 and pumps, said treatment unit including no storage tank and the eventual treatment 4 for the unfiltered flow 22.

EXAMPLES

Example 1

(20) The recirculation tank 3 contains 60 m.sup.3 of hydrochloric acid at 15% having a silicon content of roughly 59 mg.Math.L.sup.1. The acid pickles different steel grades, e.g.: interstitial steel, medium carbon, HSLA and dual phase steels. The used pickling acid is sent by pumps to the ultrafiltration device at a flow of 17 m.sup.3.Math.h.sup.1. The ultrafiltration device 2 is made of 68 m.sup.2 of ceramic membrane area having a pore size of 7 nm (10 kDa Molecular Weight). A flow of 14 m.sup.3.Math.h.sup.1 of filtered flow containing 38 mg.Math.L.sup.1 of silicon is fed back inside the bath while a flow of 3 m.sup.3.Math.h.sup.1 of unfiltered flow containing 157 mg.Math.L.sup.1.

(21) TABLE-US-00001 Flow rate Si concentration Colloidal and suspended [m.sup.3 .Math. h.sup.1] [mg .Math. L.sup.1] matter > 7 nm Entering flow 17 59 100 Filtered flow 14 38 0 Unfiltered flow 3 157 100