CN111547696A - Preparation method of optical-grade yttrium metaphosphate - Google Patents
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- CN111547696A CN111547696A CN202010413834.0A CN202010413834A CN111547696A CN 111547696 A CN111547696 A CN 111547696A CN 202010413834 A CN202010413834 A CN 202010413834A CN 111547696 A CN111547696 A CN 111547696A
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Abstract
The technical scheme of the invention provides a preparation method of optical grade yttrium metaphosphate, which comprises the following steps: preparing an ammonium dihydrogen phosphate aqueous solution, and removing water insoluble substances; removing nonferrous metals and impurity ions by an ion exchange device; and the optical grade yttrium metaphosphate can be prepared by combining the yttrium oxide and the optical grade ammonium dihydrogen phosphate solid medium-high temperature two-stage clean calcination reaction. The preparation method of the technical scheme of the invention has stronger adaptability to raw materials, and the main technical indexes of the prepared optical grade yttrium metaphosphate all meet the requirements of optical grade raw materials.
Description
Technical Field
The invention relates to the field of fine inorganic phosphorus chemical industry, in particular to a preparation method of optical-grade yttrium metaphosphate.
Background
Metaphosphate is the most stable phosphate among dibasic phosphates, and is a basic raw material for the production of phosphate glass. The high-purity metaphosphate has excellent light transmittance, so that the metaphosphate can be used as an important raw material of laser glass in a high-power laser (such as national scientific engineering-Shenguang plan) and also can be used as an important raw material of some advanced optical equipment such as camera lenses, high-definition cameras, smart phone lenses and mobile phone panel substrates. The transition metals of Fe, Co, Ni and the like can cause strong absorption of metaphosphate glass in the near ultraviolet to infrared regions, and the optical performance of the glass is influenced. Therefore, the preparation of high purity metaphosphate raw material becomes the key for manufacturing high performance laser glass and optical glass.
Rare earth elements are paid more attention from scientists and especially material experts of various countries due to unique performance and wide application, optical glass doped with rare earth ions is easy to prepare, has good optical properties, larger emission section and high quantum efficiency, is particularly used for improving the performance of optical functional glass and developing new optical functions of the glass, and rare earth becomes an indispensable important raw material. Various functional glasses doped with rare earth ions are being fully paid attention and applied in the fields of optical communication, laser protection, nonlinear optics and the like. Compared with the addition of rare earth oxide (such as yttrium oxide), the addition of rare earth metaphosphate (such as yttrium metaphosphate) into the laser glass raw material is more favorable for reducing the crystallization tendency of the glass and improving the chemical stability and mechanical strength of the glass.
Disclosure of Invention
In view of the above-mentioned current state of the art, the technical problem to be solved by the present invention is to provide a method for preparing optical grade yttrium metaphosphate, so that the prepared yttrium metaphosphate meets the requirements of manufacturing optical glass and laser glass.
In order to solve the technical problems, the technical scheme of the invention provides a preparation method of optical-grade yttrium metaphosphate, which comprises the following steps:
(1) preparing an ammonium dihydrogen phosphate aqueous solution, and removing water insoluble substances;
(2) the ammonium dihydrogen phosphate aqueous solution passes through an ion exchange device to remove nonferrous metals and impurity ions;
(3) evaporating and concentrating to obtain concentrated solution, wherein the mass fraction of ammonium dihydrogen phosphate in the concentrated solution is more than 35%;
(4) cooling and crystallizing the concentrated solution, performing centrifugal separation, drying the separated solid substance to form optical-grade ammonium dihydrogen phosphate, and combining the separated liquid with the solution subjected to ion exchange in the step (2);
(5) optical-grade ammonium dihydrogen phosphate and yttrium oxide are uniformly mixed and subjected to polymerization reaction to obtain a yttrium metaphosphate intermediate;
(6) after clean pre-crushing the yttrium metaphosphate intermediate, calcining to obtain yttrium metaphosphate powder;
(7) and (3) cleanly crushing and cleanly mixing the yttrium metaphosphate powder to obtain the finished product of the optical grade yttrium metaphosphate powder.
The yttrium oxide used in the present invention may be a special grade yttrium oxide, which means Fe2O3、CuCo, Cr, Mn, Ni and Pb 7 key impurity indexes, the total content is not more than 5ppm, wherein the total content of Co, Cr, Mn, Ni and Pb is not more than 2ppm, the content of Cu is not more than 0.2ppm, and Fe2O3Content of not more than 3ppm, Cl-The total content of sulfate radicals is not more than 100ppm, Nd2O3Content (wt.)>99.5％。
Preferably, in the step (1), the solute mass fraction of the ammonium dihydrogen phosphate aqueous solution is 7-17%. More preferably, the concentration is 8 to 14%. And a precise cloth bag filter pressing mode is adopted when water insoluble substances are removed.
Preferably, in step (2), the ion exchange device is filled with cation exchange resin and anion exchange resin, the cation exchange resin comprises one or a combination of several of 001 × 4, 741, D001, iorreisin IR120 and iorreisin 35, and the anion exchange resin comprises one or a combination of several of D202, 201 × 4, 201 × 7, D406 and D407.
Preferably, the flow rate of the ammonium dihydrogen phosphate aqueous solution passing through the ion exchange unit is 1L/min to 5L/min, and more preferably, 2L/min to 4L/min.
Preferably, in the step (3), the mass fraction of ammonium dihydrogen phosphate in the concentrated solution is 35% to 43%, and more preferably 36% to 40%.
Preferably, in the step (4), the cooling crystallization temperature is 20-30 ℃, and the crystallization time is 1-4 h. Further, the cooling crystallization temperature is 22-27 ℃, the crystallization time is 1-2.5 h, and circulating water cooling of a reaction kettle jacket or coil pipe is adopted.
Preferably, in the step (4), the separated solid matter is dried by a high-efficiency boiling dryer, wherein the air inlet temperature of the high-efficiency boiling dryer is 130-160 ℃, the tower body temperature is 115-140 ℃, the air outlet temperature is 90-110 ℃, the single feeding amount is 100-300 kg, and the drying time is 1.5-4 h. Furthermore, the air inlet temperature is 138-153 ℃, the tower body temperature is 122-138 ℃, the air outlet temperature is 95-105 ℃, the single feeding amount is 150-250 kg, and the drying time is 2-3 h. In order to ensure the product quality, the material contact part of the high-efficiency boiling dryer adopts a pure aluminum or pure titanium lining and the surface is highly polished, and the air inlet needs to be subjected to multi-stage purification treatment.
Preferably, in step (5), the molar ratio of yttrium oxide to optical grade ammonium dihydrogen phosphate is 1: (5.9-6.1) and the mixing time is 1-4 h. Furthermore, the mixing molar ratio of the yttrium oxide to the optical-grade ammonium dihydrogen phosphate is 1 (5.95-2.05), and the mixing time is 1.5-3 h. In order to mix the two materials fully and uniformly, a two-dimensional or three-dimensional mixing mode is adopted, and the contact part of the materials is subjected to plastic spraying treatment.
Preferably, in the step (5), the temperature for the polymerization reaction is 450 to 530 ℃ and the reaction time is 3 to 8 hours. Furthermore, the temperature is 470-510 ℃, and the calcining time is 4-6 h. An electric furnace calcining mode can be adopted to provide heat for the polymerization reaction, in order to ensure clean and pollution-free calcining, the material contact part in the calcining process adopts high-temperature-resistant carbon fibers, and the hearth is made of Monel alloy or Hastelloy materials.
In the process of preparing yttrium metaphosphate through solid-solid calcination reaction, if a one-stage method-high temperature calcination is directly adopted, the phenomena that materials are sintered and seriously adhered to a hearth can occur, so that the materials are difficult to peel and take out after the calcination reaction is finished. In order to solve the engineering problem, the intermediate temperature zone (450-530 ℃) is firstly adopted to calcine and deaminate most of structural water and generate polymerization to generate an intermediate of the yttrium metaphosphate, and high temperature resistant carbon fiber is used as a material contact medium to facilitate the taking out of the calcined material. However, the problem that it is difficult to completely dehydrate the yttrium metaphosphate at this temperature range, at most 96% of the structure water can be removed, and higher permanent temperature and further calcining equipment are required to remove the final small amount of structure water.
Preferably, in the step (6), the calcining temperature is 740-830 ℃, the calcining time is 3-7 h, more preferably, the calcining temperature of a high-temperature electric furnace is 760-810 ℃, and the calcining time is 4-6 h. The calcining mode of the electric furnace can be adopted, and in order to ensure clean and pollution-free calcining, the high-temperature hearth is made of high-purity corundum or high-purity quartz.
Preferably, in the step (7), a ceramic pulverizer is adopted in the process of cleanly pulverizing the yttrium metaphosphate fine powder, a two-dimensional or three-dimensional mixing mode is adopted in the process of cleanly mixing, and the mixing time is 1 h-4 h, more preferably 1.5 h-3 h. The material contact part adopts plastic spraying treatment.
The preparation method of the optical grade yttrium metaphosphate in the technical scheme of the invention has the following beneficial effects: the industrial ammonium dihydrogen phosphate is purified by adopting an ion exchange method, and the optical grade yttrium metaphosphate can be prepared by combining the yttrium oxide and the optical grade ammonium dihydrogen phosphate solid-medium-high temperature two-stage clean calcination reaction, so that the optical grade yttrium metaphosphate has strong adaptability to raw materials (the special grade yttrium oxide is a highly mature raw material in the market), and the main technical indexes of the optical grade yttrium metaphosphate can meet the requirements of the optical grade raw materials.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings required to be used in the description of the embodiments will be briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art that other drawings can be obtained according to the drawings without inventive labor.
Fig. 1 is a flow chart of a method for preparing optical grade yttrium metaphosphate according to the technical scheme of the invention.
Detailed Description
The conception, the specific structure and the technical effects of the present invention will be further described with reference to the accompanying drawings to fully understand the objects, the features and the effects of the present invention.
As shown in fig. 1, the method for preparing optical grade yttrium metaphosphate according to the present invention comprises the following steps:
(1) preparing ammonium dihydrogen phosphate aqueous solution, and removing water insoluble substances (namely, filter pressing);
(2) the ammonium dihydrogen phosphate aqueous solution passes through an ion exchange device (i.e. a cation exchange resin and an anion exchange resin in figure 1) to remove nonferrous metals and impurity ions;
(3) evaporating and concentrating (concentrating) to obtain a concentrated solution, wherein the mass fraction of ammonium dihydrogen phosphate in the concentrated solution is more than 35%;
(4) cooling and crystallizing the concentrated solution, performing centrifugal separation, drying (boiling and drying) the separated solid substance to form optical-grade ammonium dihydrogen phosphate, and combining the separated liquid with the solution subjected to ion exchange in the step (2);
(5) optical-grade ammonium dihydrogen phosphate and yttrium oxide are uniformly mixed and subjected to polymerization reaction (namely, middle-temperature clean electric furnace calcination) to obtain a yttrium metaphosphate intermediate;
(6) after the yttrium metaphosphate intermediate is cleaned and pre-crushed, calcining (namely calcining in a high-temperature clean electric furnace) to obtain yttrium metaphosphate powder;
(7) and (3) cleanly crushing and cleanly mixing the yttrium metaphosphate powder to obtain the finished product of the optical grade yttrium metaphosphate powder.
Example 1
The preparation method of the optical grade yttrium metaphosphate comprises the following steps:
(1)200kg of industrial grade ammonium dihydrogen phosphate with the content of 98 percent is dissolved in water to prepare 1508kg of ammonium dihydrogen phosphate aqueous solution with the mass fraction of 13 percent, and a micro-water insoluble substance is removed by adopting a precise cloth bag filter pressing mode;
(2) passing through a composite ion exchange device composed of 001 × 4 type cation exchange resin and IONS D202 and 201 × 4 type anion exchange resin at a flow rate of 4.3L/min to remove Fe, Mn, Pb, Cr, Cu, Ni, Co and other nonferrous metals and Cl-Sulfate radicals and the like;
(3) concentrating to 39% by evaporation;
(4) cooling the concentrated solution to 24 ℃, performing cooling crystallization and solid-liquid centrifugal separation, performing high-efficiency boiling drying on the separated crystal, wherein the air inlet temperature of a high-efficiency boiling dryer is 139-148 ℃, the tower body temperature is 123-133 ℃, the air outlet temperature is 95-101 ℃, the single feeding amount is not more than 150kg, the drying time is 2 hours, 143kg of ammonium dihydrogen phosphate is obtained, and the separated liquid is combined with the solution subjected to ion exchange in the step (2);
(5) mixing 46.6kg of special yttrium oxide and 143kg of ammonium dihydrogen phosphate in a two-dimensional mixer with an internal cavity for spraying plastics for 2 hours, calcining the mixture in an electric furnace at a medium temperature of 500 ℃ for 6 hours to obtain 138.3kg of an intermediate of yttrium metaphosphate, wherein high-temperature-resistant carbon fibers are used as material contact media in the medium-temperature calcination process, and a hearth is made of Mennel alloy;
(6) pretreating and crushing the intermediate of the yttrium metaphosphate by using a ceramic rolling machine, then calcining the crushed intermediate in a high-temperature electric furnace at the temperature of 810 ℃ for 5 hours to obtain 131.4kg of crushed yttrium metaphosphate powder, wherein the hearth of the high-temperature electric furnace adopts a high-purity corundum lining;
(7) and (3) after the yttrium metaphosphate is cleanly crushed by a ceramic crusher, mixing for 2 hours in a three-dimensional mixer with an internal cavity sprayed with plastic to obtain 130.8kg of optical grade yttrium metaphosphate finished product, and carrying out vacuum packaging with the comprehensive yield of 97.2%.
Example 2
The preparation method of the optical grade yttrium metaphosphate comprises the following steps:
(1)230kg of 97 percent industrial grade ammonium dihydrogen phosphate is dissolved in water to prepare 1859kg of 12 percent ammonium dihydrogen phosphate aqueous solution, and a micro-water insoluble substance is removed by adopting a precise cloth bag filter pressing mode;
(2) passing through a group of composite ion exchange devices composed of 741, IONRESIN IR120 type cation exchange resin and D407, D406 type anion exchange resin at a flow rate of 4.5L/min to remove Fe, Mn, Pb, Cr, Cu, Ni, Co and other nonferrous metals and Cl-Sulfate radicals and the like;
(3) evaporating, concentrating and concentrating to 40%;
(4) cooling the concentrated solution to 23 ℃, performing cooling crystallization and solid-liquid centrifugal separation, performing high-efficiency boiling drying on the separated crystal, wherein the air inlet temperature of a high-efficiency boiling dryer is 142-150 ℃, the tower body temperature is 128-135 ℃, the air outlet temperature is 100-106 ℃, the single feeding amount is not more than 180kg, and the drying time is 2.5h to obtain 165kg of ammonium dihydrogen phosphate, and combining the separated liquid with the solution subjected to ion exchange in the step (2);
(5) mixing 53.8kg of special yttrium oxide and 165kg of ammonium dihydrogen phosphate in a two-dimensional mixer with an internal cavity for spraying plastics for 2 hours, calcining the mixture at 480 ℃ in an electric furnace for 7 hours to obtain 160kg of an yttrium metaphosphate intermediate, wherein high-temperature-resistant carbon fibers are used as material contact media in the intermediate-temperature calcination process, and a hearth is made of Monel alloy;
(6) pretreating and crushing the intermediate of the yttrium metaphosphate by using a ceramic rolling machine, and then calcining the crushed intermediate in a high-temperature electric furnace at 790 ℃ for 3 hours to obtain 152kg of crushed yttrium metaphosphate powder, wherein a hearth of the high-temperature electric furnace adopts a high-purity corundum lining;
(7) and (3) after the yttrium metaphosphate is cleanly crushed by a ceramic crusher, mixing for 2.5 hours in a three-dimensional mixer with an internal cavity sprayed with plastics to obtain 151.4kg of optical grade yttrium metaphosphate finished product, and carrying out vacuum packaging, wherein the comprehensive yield is 97.5%.
Example 3
The preparation method of the optical grade yttrium metaphosphate comprises the following steps:
(1) dissolving 250kg of 98.5 percent industrial grade ammonium dihydrogen phosphate in water to prepare 1759kg of 14 percent ammonium dihydrogen phosphate aqueous solution, and removing trace water insoluble substances by adopting a precise cloth bag filter pressing mode;
(2) passing through a group of composite ion exchange devices composed of IONRESIN IR120, IONRESIN 35 type cation exchange resin and 201 × 7, 201 × 4 type anion exchange resin at a flow rate of 4.1L/min to remove Fe, Mn, Pb, Cr, Cu, Ni, Co and other nonferrous metals and Cl-Sulfate radicals and the like;
(3) evaporating, concentrating and concentrating to 40%;
(4) cooling the concentrated solution to 24 ℃, performing cooling crystallization and solid-liquid centrifugal separation, performing high-efficiency boiling drying on the separated crystal, wherein the air inlet temperature of a high-efficiency boiling dryer is 140-146 ℃, the tower body temperature is 126-132 ℃, the air outlet temperature is 99-103 ℃, the single feeding amount is not more than 200kg, and the drying time is 3 hours, so that 183.5kg of ammonium dihydrogen phosphate is obtained, and the separated liquid is combined with the solution subjected to ion exchange in the step (2);
(5) mixing 59.7kg of special yttrium oxide and 183.5kg of ammonium dihydrogen phosphate in a two-dimensional mixer with an internal cavity for spraying plastics for 3 hours, calcining the mixture at the medium temperature of 510 ℃ in an electric furnace for 5 hours to obtain 177kg of an intermediate yttrium metaphosphate, wherein high-temperature-resistant carbon fibers are used as material contact media in the medium-temperature calcination process, and a hearth is made of Mennel alloy;
(6) pretreating and crushing the intermediate of the yttrium metaphosphate by using a ceramic rolling machine, and then calcining the crushed intermediate in a high-temperature electric furnace at 800 ℃ for 4 hours to obtain 169kg of crushed yttrium metaphosphate powder, wherein a hearth of the high-temperature electric furnace adopts a high-purity corundum lining;
(7) and (3) after the yttrium metaphosphate is cleanly crushed by a ceramic crusher, mixing for 3 hours in a three-dimensional mixer with an internal cavity sprayed with plastic to obtain 168.3g of optical grade yttrium metaphosphate finished product, and carrying out vacuum packaging with the comprehensive yield of 97.7%.
Example 4
The preparation method of the optical grade yttrium metaphosphate comprises the following steps:
(1) dissolving 180kg of 98.5% industrial grade ammonium dihydrogen phosphate in water to prepare 1313kg of 13.5% ammonium dihydrogen phosphate aqueous solution, and removing trace water insoluble substances by adopting a precise cloth bag filter pressing mode;
(2) passing through a group of composite ion exchange devices composed of 741, D001, IONRISIN IR120 type cation exchange resin and 201 × 4, 201 × 7, D407 type anion exchange resin at a flow rate of 4.2L/min to remove Fe, Mn, Pb, Cr, Cu, Ni, Co and other nonferrous metals and Cl-Sulfate radicals and the like;
(3) concentrating to 39% by evaporation;
(4) cooling the concentrated solution to 24 ℃, performing cooling crystallization and solid-liquid centrifugal separation, performing high-efficiency boiling drying on the separated crystal, wherein the air inlet temperature of a high-efficiency boiling dryer is 141-149 ℃, the tower body temperature is 128-135 ℃, the air outlet temperature is 102-110 ℃, the single feeding amount is not more than 150kg, and the drying time is 2.5h to obtain 130kg of ammonium dihydrogen phosphate, and combining the separated liquid with the solution subjected to ion exchange in the step (2);
(5) mixing 42.3kg of special yttrium oxide and 130kg of ammonium dihydrogen phosphate in a two-dimensional mixer with an internal cavity for spraying plastics for 2h, calcining the mixture at 490 ℃ in an electric furnace for 6h to obtain 125.8kg of an intermediate of yttrium metaphosphate, wherein high-temperature-resistant carbon fibers are used as material contact media in the intermediate-temperature calcination process, and a hearth is made of Mennel alloy;
(6) pretreating and crushing the intermediate of the yttrium metaphosphate by using a ceramic rolling machine, and then calcining the crushed intermediate in a high-temperature electric furnace at 780 ℃ for 5 hours to obtain 120kg of crushed yttrium metaphosphate powder, wherein a hearth of the high-temperature electric furnace adopts a high-purity corundum lining;
(7) and (3) after the yttrium metaphosphate is cleanly crushed by a ceramic crusher, mixing for 2 hours in a three-dimensional mixer with an internal cavity sprayed with plastics to obtain 119.4kg of optical grade yttrium metaphosphate finished product, and carrying out vacuum packaging with the comprehensive yield of 97.8%.
Analysis of the ammonium dihydrogen phosphate formed in step (4) in the production Processes of examples 1 to 4, impurities in the composition mainly included Fe2O3Cu, Co, Cr, Mn, Ni and Pb 7 key impurity indexes, and the total content is not more than 3ppm, wherein the total content of Co, Cr, Mn, Ni and Pb is not more than 0.5ppm, the content of Cu is not more than 0.1ppm, and Fe2O3Content of not more than 1ppm, Cl-The total content of sulfate radicals is not more than 80ppm, P2O5The content is 62 +/-0.5%.
The yttrium metaphosphate samples obtained in examples 1 to 4 were analyzed, and the results are shown in Table 1:
TABLE 1 analysis of samples of yttrium metaphosphate
As can be seen from Table 1, in the yttrium metaphosphates prepared in examples 1 to 4, Fe2O3The total content of 7 key impurity indexes of Cu, Co, Cr, Mn, Ni and Pb is not more than 5ppm, wherein the total content of Co, Cr, Mn, Ni and Pb is not more than 1.5ppm, the content of Cu is not more than 0.2ppm, and Fe2O3Content of not more than 3ppm, Cl-The total content of sulfate radicals is not more than 100ppm, Y2O3Content 35 + -0.5%, P2O5The content is 65 +/-0.5%.
The optical grade yttrium metaphosphate prepared by the technical scheme of the invention has high main content, low impurity content, stable quality and uniform granularity, each index meets the index requirements of laser glass and optical glass raw materials, and the preparation method of the optical grade yttrium metaphosphate is efficient, simple and convenient, low in production cost and high in product yield.
While specific embodiments of the present invention have been described in detail above, it will be appreciated that those skilled in the art, upon attaining an understanding of the foregoing may readily produce alterations to, variations of, and equivalents to these embodiments. Therefore, the technical solutions available to those skilled in the art through logic analysis, reasoning and limited experiments based on the prior art according to the concept of the present invention should be within the scope of protection defined by the claims.
Claims (10)
1. A preparation method of optical grade yttrium metaphosphate is characterized by comprising the following steps:
(1) preparing an ammonium dihydrogen phosphate aqueous solution, and removing water insoluble substances;
(2) the ammonium dihydrogen phosphate aqueous solution passes through an ion exchange device to remove nonferrous metals and impurity ions;
(3) evaporating and concentrating to obtain concentrated solution, wherein the mass fraction of ammonium dihydrogen phosphate in the concentrated solution is more than 35%;
(4) cooling and crystallizing the concentrated solution, performing centrifugal separation, drying the separated solid substance to form optical-grade ammonium dihydrogen phosphate, and combining the separated liquid with the solution subjected to ion exchange in the step (2);
(5) optical-grade ammonium dihydrogen phosphate and yttrium oxide are uniformly mixed and subjected to polymerization reaction to obtain a yttrium metaphosphate intermediate;
(6) after clean pre-crushing the yttrium metaphosphate intermediate, calcining to obtain yttrium metaphosphate powder;
(7) and (3) cleanly crushing and cleanly mixing the yttrium metaphosphate powder to obtain the finished product of the optical grade yttrium metaphosphate powder.
2. The method of claim 1, wherein in step (1), the ammonium dihydrogen phosphate aqueous solution has a solute mass fraction of 7% to 17%.
3. The method of claim 1, wherein in step (2), the ion exchange device is filled with cation exchange resin and anion exchange resin, the cation exchange resin comprises one or more selected from 001 x 4, 741, D001, iorreisin IR120 and iorreisin 35, and the anion exchange resin comprises one or more selected from D202, 201 x 4, 201 x 7, D406 and D407.
4. The method of claim 1, wherein in step (2), the ammonium dihydrogen phosphate aqueous solution is passed through the ion exchange device at a flow rate of 1L/min to 5L/min.
5. The process of claim 1, wherein in step (3), the concentration solution comprises ammonium dihydrogen phosphate in an amount of 35 to 43% by weight.
6. The process for preparing optical grade yttrium metaphosphate according to claim 1, wherein in the step (4), the cooling crystallization temperature is 20-30 ℃ and the crystallization time is 1-4 h.
7. The method of claim 1, wherein in step (4), the separated solid material is dried by a high efficiency boiling dryer, wherein the inlet air temperature of the high efficiency boiling dryer is 130-160 ℃, the tower temperature is 115-140 ℃, the outlet air temperature is 90-110 ℃, and the drying time is 1.5-4 h.
8. The method of claim 1, wherein in step (5), the molar ratio of yttrium oxide to optical grade ammonium dihydrogen phosphate is 1 (5.9-6.1).
9. The process for preparing optical grade yttrium metaphosphate according to claim 1, wherein in step (5), the polymerization reaction is carried out at a temperature of 450 ℃ to 530 ℃ for 3 hours to 8 hours.
10. The process for preparing optical grade yttrium metaphosphate according to claim 1, wherein in step (6), the calcination temperature is 740 to 830 ℃ and the calcination time is 3 to 7 hours.
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Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB510889A (en) * | 1938-02-09 | 1939-08-09 | Du Pont | Improvements in and relating to the production of nitrous oxide |
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Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB510889A (en) * | 1938-02-09 | 1939-08-09 | Du Pont | Improvements in and relating to the production of nitrous oxide |
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| DORA ILIEVA ET AL: "Vibrational spectra of R(PO3)3 metaphosphates(R =Ga, In, Y, Sm, Gd, Dy)", 《JOURNAL OF RAMAN SPECTROSCOPY》 * |
| 孙来九: "《精细无机化工工艺学》", 31 December 1993, 西北工业大学出版社 * |
| 机械工业信息研究院/产业与市场研究所: "《中国机电产品成套设备购销手册》", 31 December 2000, 机械工业出版社 * |
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Application publication date: 20200818 |