CN204873875U - Green sulfate process titanium dioxide powder apparatus for producing - Google Patents
Green sulfate process titanium dioxide powder apparatus for producing Download PDFInfo
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- CN204873875U CN204873875U CN201520015816.1U CN201520015816U CN204873875U CN 204873875 U CN204873875 U CN 204873875U CN 201520015816 U CN201520015816 U CN 201520015816U CN 204873875 U CN204873875 U CN 204873875U
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Abstract
The utility model relates to a green sulfate process titanium dioxide powder apparatus for producing, production processes on swim over to low reaches and include in proper order: the grinding device, the acidolysis device, clarification device, vacuum crystallization device, disc filter equipment, meticulous filter equipment, the vacuum concentration device, titanium liquid preheating device, the device of hydrolysising, one washes the piece device, the making beating device, one washes the device, bleaching apparatus, two wash the device, sheet frame filter pressing device, vacuum drum dewatering device is handled to salt, sintering device, the raymond mill device, making beating dispersion devices, the sanding device, the diolame device, three wash the device, drying device, jet milling device and packing plant. The utility model discloses can not only improve the titanium white rate of recovery, the enterprise creates economic benefits for the sulfate process titanium dioxide powder, has reduced the emission of spent acid and waste water moreover, has alleviateed ambient pressure, for the society has created the environmental benefit, is a green new technology.
Description
Technical field
The utility model relates to environmental technology field, be specifically related to one and be applicable to sulfuric acid method titanium pigment industry, achieve simultaneously and improve the titanium dioxide rate of recovery, improve sulfuric acid cyclic utilization rate, the facility investment improving washing water cyclic utilization rate is few, energy consumption is low, and oil removing sulphur removal can be carried out simultaneously, the environmental protection sulfuric acid method titanium pigment production equipment that stripping efficiency is high.
Background technology
In current sulfuric acid method titanium pigment industry, titanium dioxide yield is 87-88%, and main loss derives from hydrolysis workshop section, washing workshop section, and calcining workshop section, packing department, loss amount is respectively: 4-5%, 2-3%, 1-2%, 1-2%.The loss of washing workshop section is mainly derived from the titanyl sulfate be dissolved in washing waste water, and this part loss is because CN strainer cannot retain the titanium of solubilised state.The fly-ash separator of the loss mainly rotary kiln back segment of calcining workshop section cannot trap the titanium dioxide dust in flue gas completely, causes titanium dioxide granule with fume emission; The titanium dioxide granule sprayed in spent acid is not essentially completely recovered and is namely sent to acidolysis workshop section and wastewater treatment working section in addition, and the titanium dioxide granule being sent to wastewater treatment working section is also wasted.Each producer is that a part is back to acidolysis workshop section as initiator to the mode that spent acid adopts, and a part delivers to wastewater treatment.Although there is a lot of producer to have pigment waste acid concentrator to process this part spent acid, because waste acid concentration technical strength is limited, and spent acid complicated easily causes concentrating unit to block, and makes pigment waste acid concentrator substantially idle.This part spent acid being sent to wastewater treatment obviously finally just becomes solid waste and slatterns.Sulfate process titanium dioxide powder craft is quite large to the demand of water, and conventional is two wash waters at present, three wash water reuses to are washed, and a washing water discharge, a wash water is loss water.
A lot of producer undergoes technological transformation to technique, reduces the loss of titanium dioxide, reduces the loss of spent acid, reduces the use of water, although achieve noticeable achievement, does not solve loss problem from source, so the improvement of technique still has the potential to be tapped.
Utility model content
For the problems referred to above, main purpose of the present utility model is to provide one to be applicable to sulfuric acid method titanium pigment industry, achieve simultaneously and improve the titanium dioxide rate of recovery, improve sulfuric acid cyclic utilization rate, the facility investment improving washing water cyclic utilization rate is few, energy consumption is low, and oil removing sulphur removal can be carried out simultaneously, the environmental protection sulfuric acid method titanium pigment production equipment that stripping efficiency is high.
The utility model solves above-mentioned technical problem by following technical proposals: a kind of environmental protection sulfuric acid method titanium pigment production equipment, described production equipment comprises from the most upstream of production process successively to most downstream: grinding device, acidolysis device, clarifying plant, vacuum crystallization device, disc filtration device, fine filtration device, vacuum concentrating apparatus, titanium liquid primary heater unit, hydrolysis device, one washes sheet devices, beating apparatus, one cleaning device, bleaching system, two cleaning devices, filter press device, Ficus caricaL vacuum drum dewatering unit, roasting assembly, Raymond mill device, making beating diverting device, sanding apparatus, coating device, three cleaning devices, drying installation, air flow crushing device and packing plant, described grinding device, acidolysis device, clarifying plant, vacuum crystallization device, disc filtration device, fine filtration device, vacuum concentrating apparatus, titanium liquid primary heater unit, hydrolysis device, one washes sheet devices, beating apparatus, one cleaning device, bleaching system, two cleaning devices, filter press device, Ficus caricaL vacuum drum dewatering unit, roasting assembly, Raymond mill device, making beating diverting device, sanding apparatus, coating device, three cleaning devices, drying installation, air flow crushing device is connected cooperation successively with packing plant.
In specific embodiment of the present utility model, one washes on sheet devices and is connected with spent acid membrane treatment appts.
In specific embodiment of the present utility model, a cleaning device is connected with one and washes wastewater membrane treatment unit.
In specific embodiment of the present utility model, two cleaning devices are connected with two and wash wastewater membrane treatment unit.
In specific embodiment of the present utility model, three cleaning devices are connected with three and wash wastewater membrane treatment unit.
Accompanying drawing explanation
Fig. 1 is integrated artistic schema of the present utility model;
Fig. 2 is the process flow sheet being back to acidolysis workshop section in the utility model;
Fig. 3 is useless acid-treated process flow sheet in the utility model;
Fig. 4 is the process flow sheet of weak acid plain boiled water process in the utility model;
Fig. 5 is two process flow sheets washing wastewater treatment in the utility model;
Fig. 6 is the process flow sheet calcining tail gas wastewater treatment in the utility model;
Fig. 7 is three process flow sheets washing wastewater treatment in the utility model.
Embodiment
The utility model preferred embodiment is provided, to describe the technical solution of the utility model in detail below in conjunction with accompanying drawing.
Fig. 1 is integrated artistic schema of the present utility model.As shown in Figure 1, the most upstream of the device production process adopted in the utility model comprises successively to most downstream: grinding device, acidolysis device, clarifying plant, vacuum crystallization device, disc filtration device, fine filtration device, vacuum concentrating apparatus, titanium liquid primary heater unit, hydrolysis device, one washes sheet devices, beating apparatus, one cleaning device, bleaching system, two cleaning devices, filter press device, Ficus caricaL vacuum drum dewatering unit, roasting assembly, Raymond mill device, making beating diverting device, sanding apparatus, coating device, three cleaning devices, drying installation, air flow crushing device and packing plant.
One washes on sheet devices and is connected with spent acid membrane treatment appts, a cleaning device is connected with one and washes wastewater membrane treatment unit, two cleaning devices are connected with two and wash wastewater membrane treatment unit, three cleaning devices are connected with three and wash wastewater membrane treatment unit.
What adopt in the utility model is that wet arizonite produces rutile titanium dioxide, and its workshop section is followed successively by: grinding, acidolysis, clarification, vacuum crystallization, disk filtration, fine filtering, vacuum concentration, the preheating of titanium liquid, hydrolysis, are washed slice, making beating, is washed, bleach, two wash, the dehydration of filter press, Ficus caricaL vacuum drum, calcining, Raymond mill, making beating dispersion, sand milling, coating, three are washed, drying, comminution by gas stream, packaging.
Wherein a Xi Shangpian workshop section adds spent acid membrane treatment process, one washes workshop section adds one and washes wastewater membrane treatment process, two wash workshop section adds two and washes wastewater membrane treatment process, calcining workshop section adds calcining tail gas wastewater membrane treatment process and sulphuric acid concentration technique, and three wash workshop section adds three and wash wastewater membrane treatment process.
In the utility model, one washes a spent acid produced need through film process, the dope of the metatitanic acid particle in waste acid recovery and sulfur acid ferrous iron and titanyl sulfate, and produce clean dilute sulphuric acid, spent acid need comprise the microfiltration membrane process of leading portion and the resistance to sorrel process of back segment through film process, the dope containing metatitanic acid that microfiltration membrane process produces returns one and washes film trap, and clear liquid enters resistance to sorrel; The sulfur acid that resistance to sorrel process produces dope that is ferrous and titanyl sulfate returns acidolysis workshop section, and the clean dilute sulphuric acid produced makes the spray liquid of calcining kiln tail gas.
In the utility model, the metatitanic acid solid act as in interception spent acid of microfiltration membrane, microfiltration membrane precision used is 50-500 nanometer, and transmembrane pressure is 0.05-0.8MPa; The acting as of resistance to sorrel retains ferrous sulfate in spent acid and titanyl sulfate, allow sulfuric acid through, resistance to sorrel used is 85-98% to the rejection of ferrous ion, is 80-95% to the rejection of titanyl sulfate, resistance to sulfuric acid concentration is 0-30%, and working pressure is 1.5-4.5MPa.
In the utility model, the weak acid plain boiled water washing generation need through film process, with the metatitanic acid particle reclaimed in plain boiled water and sulfur acid is ferrous and the dope of titanyl sulfate, and produces the diluted acid water cleaned.
The process of plain boiled water film comprises the microfiltration membrane process of leading portion and the resistance to sorrel process of back segment, and the dope containing metatitanic acid that microfiltration membrane process produces returns a washing trough, and clear liquid enters resistance to sorrel; The sulfur acid that resistance to sorrel process produces dope that is ferrous and titanyl sulfate returns acidolysis workshop section, and the clean diluted acid water of generation is made a wash water and recycled.
The metatitanic acid solid act as in interception spent acid of microfiltration membrane, microfiltration membrane precision used is 50-500 nanometer, and transmembrane pressure is 0.05-0.8MPa; The acting as of resistance to sorrel retains ferrous sulfate in spent acid and titanyl sulfate, allow sulfuric acid through, resistance to sorrel used is 85-98% to the rejection of ferrous ion, is 80-95% to the rejection of titanyl sulfate, resistance to sulfuric acid concentration is 0-30%, and working pressure is 1.5-4.5MPa.
In the utility model, two wash two of generation wash waste water need through film process, with the metatitanic acid particle reclaimed in waste water and sulfur acid is ferrous and the dope of titanyl sulfate, and produce the diluted acid water cleaned.
Two wash wastewater membrane process comprises the microfiltration membrane process of leading portion and the resistance to sorrel process of back segment, and the dope containing metatitanic acid that microfiltration membrane process produces returns two washing troughs, and clear liquid enters resistance to sorrel; The sulfur acid that resistance to sorrel process produces dope that is ferrous and titanyl sulfate returns acidolysis workshop section, and the clean diluted acid water of generation is made two wash waters and recycled.
The metatitanic acid solid act as in interception spent acid of microfiltration membrane, microfiltration membrane precision used is 50-500 nanometer, and transmembrane pressure is 0.05-0.8MPa; The acting as of resistance to sorrel retains ferrous sulfate in spent acid and titanyl sulfate, allow sulfuric acid through, resistance to sorrel used is 85-98% to the rejection of ferrous ion, is 80-95% to the rejection of titanyl sulfate, resistance to sulfuric acid concentration is 0-30%, and working pressure is 1.5-4.5MPa.
Two wash and need supplementary deionized water, and amount of makeup water is the 0-30% of two leaching requirements.
In the utility model, come from dilute sulphuric acid that the spent acid to wash slice produces after the microfiltration membrane process tail gas spray liquid as calcining kiln, the waste liquid produced after spray need through film process, with the titanium dioxide granule in Recycling of waste liquid, and producing clean dilute sulphuric acid, dilute sulphuric acid enters sulphuric acid concentration device.
The titanium dioxide solids act as in interception spray waste liquid of microfiltration membrane, the titanium dioxide solids be blocked is back to calcining kiln, the condensation diluted acid water that sulphuric acid concentration device produces is back to a wash water groove and does a wash water use, and the vitriol oil that sulphuric acid concentration device produces is back to acidolysis workshop section.
Microfiltration membrane precision used is 50-500 nanometer, and transmembrane pressure is 0.05-0.8MPa.The concentration of the vitriol oil that sulphuric acid concentration device produces is 50-96%.
One washes and needs supplementary deionized water, and amount of makeup water is the 0-30% of a leaching requirement.
In the utility model, three wash three of generation wash waste water need through film process, reclaim the dope of titanium dioxide granule in waste water and contains sodium sulfate, and produce clean de-salted water.
Three wash wastewater membrane process comprises the microfiltration membrane process of leading portion and the reverse osmosis membrane processing of back segment, and the dope containing titanium dioxide that microfiltration membrane process produces returns three washing troughs, and clear liquid enters reverse osmosis membrane; The contains sodium sulfate dope that reverse osmosis membrane processing produces delivers to treatment and finishing section, and the de-salted water produced is made three wash waters and recycled.
The metatitanic acid solid act as in interception spent acid of microfiltration membrane, microfiltration membrane precision used is 50-500 nanometer, and transmembrane pressure is 0.05-0.8MPa; Reverse osmosis membrane act as the sodium sulfate retained in waste water, only allow water through, the ratio of desalinization of reverse osmosis membrane is 95-99%.
Three wash and need supplementary deionized water, and amount of makeup water is the 0-30% of three leaching requirements.
The treatment and finishing section of sodium sulfate is that discharge, recovery or partial discharge are partially recycled.
In the utility model, the one weak acid plain boiled water and two washing generation wash two of generation wash waste water both can individual curing as described above, also can merge or the process of process sleeve rear employing film, the dope of the metatitanic acid particle in recovery waste water and sulfur acid ferrous iron and titanyl sulfate, and produce clean diluted acid water.
Merge wastewater membrane process and comprise the microfiltration membrane process of leading portion and the resistance to sorrel process of back segment, the dope containing metatitanic acid that microfiltration membrane process produces returns a washing trough, and clear liquid enters resistance to sorrel; The sulfur acid that resistance to sorrel process produces dope that is ferrous and titanyl sulfate returns acidolysis workshop section, and the clean diluted acid water produced makes a wash water and two wash waters recycle.
The metatitanic acid solid act as in interception spent acid of microfiltration membrane, microfiltration membrane precision used is 50-500 nanometer, and transmembrane pressure is 0.05-0.8MPa; The acting as of resistance to sorrel retains ferrous sulfate in spent acid and titanyl sulfate, allow sulfuric acid through, resistance to sorrel used is 85-98% to the rejection of ferrous ion, is greater than 80-95% to the rejection of titanyl sulfate, resistance to sulfuric acid concentration is 0-30%, and working pressure is 1.5-4.5MPa.
Fig. 2 is the process flow sheet being back to acidolysis workshop section in the utility model.As shown in Figure 2: come from the vitriol oil that pigment waste acid concentrator produces, and come from and wash a spent acid film process, and wash wastewater membrane process and two and wash that the sulfur acid after wastewater membrane process is ferrous, the dope of titanyl sulfate, be all back to acidolysis workshop section.
Fig. 3 is useless acid-treated process flow sheet in the utility model.As shown in Figure 3: one washes a spent acid membrane treatment process produced comprises the microfiltration membrane process of leading portion and the resistance to sorrel process of back segment, and the dope containing metatitanic acid that microfiltration membrane process produces returns one and washes film trap, and clear liquid enters resistance to sorrel; The sulfur acid that resistance to sorrel process produces dope that is ferrous and titanyl sulfate returns acidolysis workshop section, and the clean dilute sulphuric acid produced makes the spray liquid of calcining kiln tail gas.
Fig. 4 is the process flow sheet of weak acid plain boiled water process in the utility model, as shown in Figure 4: a weak acid plain boiled water film process of washing generation comprises the microfiltration membrane process of leading portion and the resistance to sorrel process of back segment, the dope containing metatitanic acid that microfiltration membrane process produces returns a washing trough, and clear liquid enters resistance to sorrel; The sulfur acid that resistance to sorrel process produces dope that is ferrous and titanyl sulfate returns acidolysis workshop section, and the clean diluted acid water of generation is made a wash water and recycled.
Fig. 5 is two process flow sheets washing wastewater treatment in the utility model.As shown in Figure 5: two wash wastewater membrane process comprises the microfiltration membrane process of leading portion and the resistance to sorrel process of back segment, the dope containing metatitanic acid that microfiltration membrane process produces returns two washing troughs, and clear liquid enters resistance to sorrel; The sulfur acid that resistance to sorrel process produces dope that is ferrous and titanyl sulfate returns acidolysis workshop section, and the clean diluted acid water of generation is made two wash waters and recycled.
Fig. 6 is the process flow sheet calcining tail gas wastewater treatment in the utility model, as shown in Figure 6: come from the spray of the dilute sulphuric acid after washing spent acid film process calcining tail gas, produce calcining tail gas waste water.The titanium dioxide solids of waste water in film process interception spray waste liquid, the titanium dioxide solids be blocked is back to calcining kiln, and the clear liquid that film process produces is dilute sulphuric acid, and dilute sulphuric acid enters sulphuric acid concentration device.The condensation diluted acid water that sulphuric acid concentration device produces is back to a wash water groove and does a wash water use, and the vitriol oil that sulphuric acid concentration device produces is back to acidolysis workshop section.
Fig. 7 is three process flow sheets washing wastewater treatment in the utility model, as shown in Figure 7: three wash wastewater membrane process comprises the microfiltration membrane process of leading portion and the reverse osmosis membrane processing of back segment, the dope containing titanium dioxide that microfiltration membrane process produces returns three washing troughs, and clear liquid enters reverse osmosis membrane.The contains sodium sulfate dope that reverse osmosis membrane processing produces delivers to treatment and finishing section, and the de-salted water produced is made three wash waters and recycled.
Embodiment one
One to wash titanium concentration in a spent acid be 9.22g/L, and ferrous ion concentration is 45g/L, and sulfuric acid content is 20%.This spent acid is first through microfiltration membrane process, and microfiltration membrane precision is 200nm, and transmembrane pressure is 0.2MPa.Return one containing the dope of metatitanic acid after film process and wash film trap, after film process, in clear liquid, titanium concentration is 2g/L.Clear liquid after microfiltration membrane process continues to adopt resistance to sorrel process, and working pressure is 3.8MPa.After resistance to sorrel process, sulfur acid dope that is ferrous and titanyl sulfate is back to acidolysis pot, and in the clear liquid after the resistance to sorrel process of single-stage, titanium concentration is 140mg/L, and ferrous ion concentration is 2.25g/L, and sulfuric acid content is 20%; In clear liquid after the resistance to sorrel process of two-stage, titanium concentration is 9.8mg/L, and ferrous ion concentration is 112mg/L, and sulfuric acid content is 20%.This clear liquid is sent to calcining kiln as calcining tail gas spray liquid.
From film processing efficiency, microfiltration membrane is more than 99% to the intercepting efficiency of metatitanic acid, and remaining titanium is then deliquescent titanium (titanyl sulfate).The resistance to sorrel of single-stage is 95% to the rejection of ferrous ion, is 93% to the rejection of titanyl sulfate.
More than show and describe ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications; these changes and improvements all fall within the scope of claimed the utility model, and the claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (5)
1. an environmental protection sulfuric acid method titanium pigment production equipment, it is characterized in that: described production equipment comprises from the most upstream of production process successively to most downstream: grinding device, acidolysis device, clarifying plant, vacuum crystallization device, disc filtration device, fine filtration device, vacuum concentrating apparatus, titanium liquid primary heater unit, hydrolysis device, one washes sheet devices, beating apparatus, one cleaning device, bleaching system, two cleaning devices, filter press device, Ficus caricaL vacuum drum dewatering unit, roasting assembly, Raymond mill device, making beating diverting device, sanding apparatus, coating device, three cleaning devices, drying installation, air flow crushing device and packing plant, described grinding device, acidolysis device, clarifying plant, vacuum crystallization device, disc filtration device, fine filtration device, vacuum concentrating apparatus, titanium liquid primary heater unit, hydrolysis device, one washes sheet devices, beating apparatus, one cleaning device, bleaching system, two cleaning devices, filter press device, Ficus caricaL vacuum drum dewatering unit, roasting assembly, Raymond mill device, making beating diverting device, sanding apparatus, coating device, three cleaning devices, drying installation, air flow crushing device is connected cooperation successively with packing plant.
2. environmental protection sulfuric acid method titanium pigment production equipment according to claim 1, is characterized in that: one washes on sheet devices and is connected with spent acid membrane treatment appts.
3. environmental protection sulfuric acid method titanium pigment production equipment according to claim 1, is characterized in that: a cleaning device is connected with one and washes wastewater membrane treatment unit.
4. environmental protection sulfuric acid method titanium pigment production equipment according to claim 1, is characterized in that: two cleaning devices are connected with two and wash wastewater membrane treatment unit.
5. environmental protection sulfuric acid method titanium pigment production equipment according to claim 1, is characterized in that: three cleaning devices are connected with three and wash wastewater membrane treatment unit.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201520015816.1U CN204873875U (en) | 2015-01-09 | 2015-01-09 | Green sulfate process titanium dioxide powder apparatus for producing |
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| CN201520015816.1U CN204873875U (en) | 2015-01-09 | 2015-01-09 | Green sulfate process titanium dioxide powder apparatus for producing |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110002495A (en) * | 2019-05-24 | 2019-07-12 | 江苏特丰新材料科技有限公司 | A kind of energy conservation and environmental protection sulfate process titanium dioxide powder producing method |
| CN110040775A (en) * | 2019-05-24 | 2019-07-23 | 江苏特丰新材料科技有限公司 | A kind of preparation method of the unformed titanium dioxide of low-sulfur |
| CN108178188B (en) * | 2018-03-08 | 2020-02-11 | 四川龙蟒钛业股份有限公司 | Method for effectively improving disc filtration efficiency and titanium liquid concentration |
-
2015
- 2015-01-09 CN CN201520015816.1U patent/CN204873875U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108178188B (en) * | 2018-03-08 | 2020-02-11 | 四川龙蟒钛业股份有限公司 | Method for effectively improving disc filtration efficiency and titanium liquid concentration |
| CN110002495A (en) * | 2019-05-24 | 2019-07-12 | 江苏特丰新材料科技有限公司 | A kind of energy conservation and environmental protection sulfate process titanium dioxide powder producing method |
| CN110040775A (en) * | 2019-05-24 | 2019-07-23 | 江苏特丰新材料科技有限公司 | A kind of preparation method of the unformed titanium dioxide of low-sulfur |
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Address after: 201201 Shanghai, Pudong New Area Jin Tang Road, No. 2, block B, 145 Patentee after: SHANGHAI ANHORN ENVIRONMENTAL TECHNOLOGY CO., LTD. Address before: 201201 Shanghai, Pudong New Area Jin Tang Road, No. 2, block B, 145 Patentee before: Shanghai Anhorn Mechanical Equipment Co., Ltd. |