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PRELIMINARY FEASIBILITY STUDY FOR THE BALTIC PHOSPHATE PROJECT Developed by the company BALTIC PHOSPHATE OÜ Developers: D. Nikulin Estonia Azeri 2023 Content Section Section name Page number 1. Introduction 3–4 2. General principles of project implementation 5–6 2.1. Project Structure 5–6 2.2. Land relations 6 3. Prerequisites for the implementation of the Project 6-9 3.1. Market preconditions 6–8 3.2. Environmental background 8-9 3.3. Geopolitical background 9 3.4. Social background 9 4. Technological solutions 9 - 14 4.1. Sulfuric acid production 9 -12 4.2. Production of extractive phosphoric acid 13 – 14 4.3. By-products of production 14 4.4. Best Available Techniques 14 5. Main technical and economic indicators of the project 14 - 17 5.1. Estimated production capacity 14 5.2. Capital expenditures 14 5.3. Operating costs 15 5.4. conservative approach 15-16 5.5. Enlarged feasibility study 16 5.6. Calculation of the number of personnel 17 6 List of used literature 18 2  1. Introduction Baltic Phosphate OU has launched a comprehensive innovative Project in the north-eastern region of Estonia for the construction of a production complex for the production of phosphoric acid (hereinafter referred to as the Project) with a phased transition to the use of raw materials (phosphorites) from local production. The construction of the production complex is envisaged on the territory of the Aseri Industrial Park. Image 1. Current status of the Aseri The project provides for the maximum use of industrial buildings, structures, engineering, and transport infrastructure currently existing in the Aseri industrial park Aseri Industrial Park is located on the seashore along the Tallinn-St. Petersburg highway at 125 km from Tallinn, 55 km from the port of Sillamäe, 85 km from Narva, 28 km from Kohtla-Järve (Pictures 2 and 3) 3 Image 2. Port of Aseri on the map of Europe Image 3. Port of Aseri on the map of Estonia 4  2. General principles for the implementation of the Project 2.1. Project structure The proposed Project for implementation involves the implementation of several subprojects. Subproject №1. Construction of a shop for the production of sulfuric acid with a power unit with a capacity of 12 MW Production capacity: • for 93% sulfuric acid - 300,000 tons per year for own production needs in the production of phosphoric acid • for electricity - 85,822,702 kWh per year, which fully meets the need for electricity of the entire production complex, with the possibility of selling the surplus through the Estonian energy system • for thermal energy - 312,734 Gcal per year to produce electricity and the provision of thermal energy to the entire production complex Investment volume – 28 750 000 EUR Subproject №2. Construction of a workshop for the production of one stripped off extractive phosphoric acid (EPA) Productive capacity: • for stripped down 85% EPA - 150,000 tons per year Investment volume – 14 700 000 EUR Subproject №3. Construction of railway sidings The subproject provides for the laying of railway access roads to the production site. Investment volume – 4 500 000 EUR Subproject №4. Construction of an electrical substation The subproject provides for its own electrical substation with a capacity of 4 MW. Investment volume – 1 150 000 EUR Subproject №5. Construction of household, transport and engineering infrastructure facilities The subproject provides for the construction of administrative and auxiliary buildings and structures, transport and engineering infrastructure of the production site of the complex, incl. autonomous wastewater treatment system. Investment volume – 4 650 000 EUR 5 Subproject №6. Implementation of measures for storage or processing of phosphogypsum The subproject provides for the implementation of the necessary measures for the storage of a product associated with the production of phosphoric acid - phosphogypsum, with the further creation of capacities for its processing. Investment volume – 3 500 000 EUR 2.2. Land relations To accommodate the production complex, the project provides for the purchase of two land plots with a total area of 20 hectares (11 hectares and 9 hectares). Investment volume – 1 350 000 EUR 3. Prerequisites for the implementation of the Project 3.1. Market preconditions 3.1.1. Applications Phosphoric acid (H3PO4) is the leading inorganic acid produced and consumed in terms of production value, and it is the second largest and by volume after sulfuric acid. Phosphoric acid is the leading intermediate or processing step between phosphate rock and end markets for phosphorus in the form of phosphate. The largest use of phosphoric acid is in the production of phosphate chemicals, consumed mainly as phosphorus carriers in fertilizers. Use in the production of animal feed is of secondary importance. Phosphoric acid is also used in the manufacture of phosphate chemicals for use in water purifiers and detergents, dentifrices, firefighting chemicals, and for a variety of smaller markets. The consumption of phosphoric acid due to its acidic properties is relatively small (for example, treatment of metal surfaces, acidification of drinks).c 6  Food, technical and other areas; 10%; 10% Other types of DAP; 35%; 35% fertilizers;; 21% TSP; 7%; 7% MAP; 27%; 27% DAP MAP TSP Other types of fertilizers Food, technical and other areas Image 4. The main applications of phosphoric acid 3.1.2. Phosphoric acid production The world production of phosphoric acid is more than 40 million tons of P2O5 per year The ten largest producers of phosphoric acid account for about 45% of the total world capacity. Basically, these are integrated companies located near sources of raw materials (deposits of phosphorus-containing ores). The Moroccan company OCP leads the world ranking, which is quite natural, since Morocco has the world's largest deposits of phosphorus-containing ores, North American Mosaic is in second place, and Canadian PotashCorp is third, although it should be noted that the Chinese Yunnan Yuntianhua International Chemical Co. practically approached the Canadian leader in terms of volume. This list also includes the Russian company Phosagro. Encouraged by the rapid growth of the Chinese economy and the growing need for phosphate fertilizers, China has become the world's largest producer and consumer of phosphoric acid. From 2008 to 2018, China's phosphoric acid output grew by an average of 3.1% per year. Production and consumption of phosphoric acid grew at an annual average of 4.5% and 4.6%, respectively, over the same period. China's production and consumption of phosphoric acid is projected to experience slower but moderate growth between 2018 and 2023. Older phosphoric acid plants in regions without local phosphate rock reserves are expected to come under additional pressure and eventually be forced to shut down. Some manufacturers in Spain, Belgium, Japan and the US have announced the closure of outdated and unprofitable plants. Most of the new phosphoric acid production facilities will be integrated into industrial complexes to produce phosphate fertilizers. As phosphate reserves are exploited in Kazakhstan and Turkmenistan, new phosphoric acid plants have been built in these two countries. The new plant is expected to be operational by 2020 in Dorogobuzh, Russia. 7  3.1.3. Phosphoric acid market The main market for phosphoric acid is the production of phosphate fertilizer products - ammonium phosphates and triple superphosphates. NO PHOSPHORUS, NO FOOD! This statement was made by a group of researchers from Australia and Sweden. According to their calculations, there is a fear that due to the growth of the world population, fertilizer production may peak by 2033, and then a decline in production will begin due to a decrease in natural reserves of phosphorus and, accordingly, a rapid increase in prices for phosphate fertilizers. The production of fertilizers accounts for about 80% of the global market for phosphoric acid and animal feed, about 6%. The rest is consumed in various industrial applications. The growth dynamics of phosphoric acid consumption over the past six years is shown below in 5 Image. Image 5. World consumption of phosphoric acid With the countries of the Asia-Pacific region, especially China and India, heavily investing in phosphate fertilizer production capacity, this region dominates the regional markets for phosphoric acid and its phosphate derivatives. This trend is expected to continue over the next six years. In addition to the Asia-Pacific region, markets in regions such as the Middle East, Africa and Latin America are growing at an astonishing rate. The phosphoric acid market in countries such as Brazil, Argentina, South Africa, Algeria, Sudan, Nigeria, Jordan, Saudi Arabia, Egypt, Iran, Yemen, Bahrain, Qatar, Kuwait and Israel is expected to grow rapidly over the coming some years. Moreover, the North American and European markets are forecast to generate strong demand for phosphoric acid as these markets gradually recover from the economic crisis. With such a positive outlook, the global phosphoric acid market is expected to maintain excellent growth rates going forward. Overall and globally, the phosphoric acid market is expected to grow by almost 4% per year. 8  3.2. Environmental background EU countries are preparing to adopt new regulations setting limits on the content of cadmium in phosphate fertilizers. The EU intends to impose restrictions on the use of phosphate fertilizers with a high content of cadmium. The compounds of this mineral are indeed extremely toxic and, accumulating in the soil, can, according to European experts, lead to sad consequences for European agriculture and human health. Phosphorites for the production of fertilizers in the EU receive mainly from Morocco - almost 1.9 million tons annually. The content of cadmium in Moroccan phosphorites is up to 30 mg/kg, which is much higher than the threshold values that Europe intends to declare as maximum permissible at one of the stages of introducing new fertilizer quality standards. The boundary value of its content can be reduced to 20 milligrams per kilogram. The projected production complex involves the processing of Syrian phosphorites grade 63-65 BPL. The content of cadmium in this raw material is not more than 8 mg/kg, which meets the new EU requirements for the maximum content level. After the start of mining of Estonian phosphorites, which meet EU standards in terms of cadmium content, production will switch to the processing of local raw materials. The start of mining of Estonian phosphate rock is scheduled for 2023 and will be implemented as part of a separate project. 3.3. Geopolitical background Of the existing exporters of fertilizers to the EU, only Russian phosphorites and fertilizers contain Cd that does not exceed the limit of 20 mg per 1 kg of phosphorus. Producers and exporters of phosphate fertilizers fear a possible Russian dominance in the European market following the introduction of new EU regulations. The launch of phosphoric acid production under the Project will partially meet the needs of the European market. 3.4. Social background The production complex under construction involves the creation of 325 new jobs. Taking into account the negative situation with unemployment in the area where production is planned to be organized, the local leadership, during the preliminary negotiations, expressed full support for the implementation of the Program. From January 1, 2019, the state began to support the creation of new jobs in the northeast and southeast of Estonia Within the framework of this program, employers can apply at the unemployment insurance fund for a job creation allowance in the north-east and south-east of Estonia. The purpose of the grant is to contribute to the economic development of these regions and to attract unused labor force to work. The allowance consists of a salary allowance and compensation for tuition costs. 4. Technological solutions 4.1. Sulfuric acid production 4.1.1. Raw materials to produce sulfuric acid The raw material for the production of sulfuric acid is sulfur, a by-product of the desulfurization processes of gas and oil refineries. Sulfur grades that are mainly used for the production of sulfuric acid are shown in Table 1. 9 Table 1 Index Variety 9998 Variety 9995 Variety 9990 Mass fraction of sulfur, %, not less than 99,98 99,95 99,90 Mass fraction of ash, %, no more 0,02 0,03 0,05 Lower quality sulfur (grades 9950 and 9920) is rarely used in the production of sulfuric acid. Sulfuric acid plants can use liquid, lump or granular sulfur. The project provides for the use of lump sulfur, imported from Kazakhstan and Russia. 4.1.2. Double contact sulfuric acid system with double absorption and absorption heat recovery For the production of sulfuric acid, it is planned to use a double contact double absorption sulfuric acid system (DKDA) and absorption heat recovery DKDA is the most common method for the production of sulfuric acid in the world. The main feature of this type of technological solutions is the presence of the stage of intermediate extraction of SO3 from the process gas. This organization of the process makes it possible to increase the overall degree of conversion of SO2 to SO3 up to 99.5% - 99.9%. The general advantages of DKDA systems are: • overall efficiency and knowledge of technological solutions; • do not require the purchase of additional raw materials and materials; • absence of liquid wastewater and, accordingly, additional costs for their treatment and neutralization; • high working time funds of technological systems and individual equipment; • relatively low operating temperatures of working media; • Easy start and stop. There is no fundamental performance limitation for systems with absorption heat recovery. The applicability of this technology is determined by technical and economic efficiency. Image 6 shows a schematic diagram of the production of sulfuric acid by the DKDA method. Image 6. Variant of the implementation of the technological scheme for the production of sulfuric acid by the DKDA method 10 1 - sulfur furnace; 2 - waste heat boiler; 3 - contact device; 4 - superheater of the 2nd stage; 5 - gas heat exchanger; 6 - gas heat exchanger; 7 — economizer of the 2nd stage; 8 - gas heat exchanger; 9 - superheater and economizer of the 1st stage in one housing; 10 - supercharger; 11 - drying tower; 12 - the first monohydrate absorber; 13 - second monohydrate absorber; 14 - circulation collector of the second monohydrate absorber; 15 - acid refrigerators; 16 a/b - combined circulation collector of the drying tower and the first monohydrate absorber; 17 - production collection; 18 - exhaust pipe; 19 - acid pumps In order to improve the overall energy efficiency of sulfuric acid production, it is planned to include an absorption heat recovery system in the technological cycle Absorption heat recovery systems are installed at the site of the first monohydrate absorber in DKDA systems. To obtain steam with a pressure of 0.6-1.0 MPa, the temperature of sulfuric acid in the cycle of the absorption heat recovery plant must be increased to 215 °C - 225 °C, which requires the use of equipment (collector, boiler, refrigerator, acid pump and acid pipelines) , made of special corrosion- resistant steels, while it is necessary to accurately maintain the concentration of sulfuric acid with a high temperature in a very narrow range (99.1–99.6 wt.%). To implement this process, additional heat exchange equipment (heat recovery boiler and heat exchangers) and an absorber of a special design are installed in the drying-absorption department. Low-grade steam generated in this technological process can be used for the needs of the enterprise. Options for including absorption heat recovery systems in a sulfuric acid plant are shown in images 7(a) and 7(b). Image 7(a). The second option for absorption heat recovery plants: 1 - absorption tower; 2 - pump for pumping hot acid; 3 - waste heat boiler; 4 - device for diluting acid; 5 - feed water heater 11 Image 7(b) Second option for absorption heat recovery plant: 1 - absorption tower; 2 - collection of hot sulfuric acid with a circulation pump; 3 - waste heat boiler; 4 - feed water heater 4.2. Production of extractive phosphoric acid (EPA) 4.2.1. The main raw material for the production of EPA The main raw materials for the production of EPA are phosphorite concentrate and sulfuric acid. Sulfuric acid for EPA production will come from the sulfuric acid plant. The need for phosphorite concentrate will be covered by: • at the first stage - due to import deliveries from Syria • at the second stage - due to the supply of local phosphorite concentrate of our own production after the development of the Estonian phosphorite deposit and the construction of the processing plant, which will significantly improve the economic performance of the project 4.2.2. Description of the applied EPA production technology For the production of EPA, the project provides for the use of the Dihydrate (DG) method. The DG process is used in almost all enterprises producing EPA. The process makes it possible to obtain EPA with a P2O5 content of 24% - 28%, is characterized by a high technological yield of P2O5 in EPA and is implemented at relatively low temperatures - 75 °C - 85 °C. EPA concentration takes place on single-vessel vacuum evaporators. The main feature of the DG method for producing EPA is the decomposition of phosphate raw materials with a mixture of sulfuric and phosphoric acids with the crystallization of calcium sulfate in the form of a stable phase - CaSO4 2H2O dihydrate. 12 A typical technological scheme of the DG.process is shown in the image 8. Image 8. Schematic diagram of the DG process for the production of EPA with vacuum cooling of the pulp The general advantages of the DG method are: • practical absence of restrictions on the quality of used phosphate raw materials; • high working time funds of technological systems and separate equipment; • relatively low operating temperatures of working media; • easily adjustable start and stop; • relatively low emission of fluorine gases at the stages of extraction-filtration; • absence of encrustation plugging of phosphogypsum removal lines when using the hydrotransport method. • economic and practical feasibility • maximum simplicity of the process. • the possibility of varying productivity, stage-by-stage increase in the level of production. • advantage if EPA concentration is not required for processing into final products. • The technology is characterized by relative ease of implementation and operation. 4.2.3 By-products of production 4.2.3.1. Phosphogypsum An inevitable by-product of the production of EPA by the sulfuric acid method is calcium sulfate dihydrate, which, due to the presence of impurity compounds of phosphorus, is called phosphogypsum (PG) As a result of the production of the amount of EPA provided by the project, it is expected to receive about 533,000 tons of FG. 4.2.3.2 Main areas of FG use 13  Having studied the analytics of FG utilization methods in the world, it is possible to determine the following areas for the use of FG: • Agriculture - as a calcium-containing chemical ameliorant. • Soil gypsum (used in USA and India) • Filling of exhausted mines, ie. filling with phosphogypsum the mined-out spaces of the mines, which to a certain extent will ensure the restoration of the strength of the rocks and exclude the possibility of their shift underground. • In the production of cement • Discharge into water (the method is widely used in Western Europe) • Manufacture of building materials, incl. bricks grade 150-200 by semi-dry pressing Production of gypsum binders • Application of FG for the production of sulfuric acid (Germany, Austria, South Africa and Poland) Specialists of Baltic Phosphate OU are currently negotiating with the Estonian Environmental Service to find an optimal solution for the use of FG. 4.3 Best Available Techniques This section presents traditional technological solutions that are preliminary. The final technological solutions to be used in this project will take into account the latest advances in technology and hardware in order to obtain the most energy efficient and environmentally friendly production. 5. Main technical and economic indicators of the project 5.1. Estimated production capacity The project assumes the creation of the following production facilities, at the rate of 330 working days per year: • for 93% sulfuric acid - 300,000 tons per year • for EPA - 150,000 tons of 85% EPA per year 5.2. Capital expenditures Table 2 Object Total cost, EUR Acquisition of land 1 350 000 Workshop for the production of sulfuric acid with a power unit with a capacity of 12 MW 28 750 000 Workshop for the production of evaporated 85% EPA 14 700 000 Administrative and auxiliary buildings 3 500 000 Engineering infrastructure of the industrial site 1 150 000 Electrical substation 1 150 000 Implementation of measures for storage or processing of phosphogypsum 3 500 000 Construction of railway tracks 4 500 000 Total 58 600 000 Contingency (10%) 5 860 000 TOTAL CAPEX 64 460 000 14 5.3. Operating costs Table 3 Quantity per Price, Sum, Description Unit year EUR/unit EUR per year Acquisition of phosphorite concentrate ton 297 000 95,00 28 215 000 29% Р2О5 Lump sulfur 99.9% ton 82 561 95,00 7 843 367 Water m3 885 498 0,75 664 123 Salary fund people 325 1 500 5 850 000 Depreciation 5% per year 3 223 000 Other costs 10% 4 257 000 TOTAL operating costs 50 052 740 5.4. Conservative approach When calculating the economic indicators of the Project, the developers applied a conservative approach in terms of: • the cost of selling phosphoric acid is assumed to be 5% lower than the weighted average price for the last 6 months of the market price (image 9) • the cost of the main raw material - lump sulfur and phosphorite concentrate, is assumed to be 3% higher than the current market price 15 Image 9. Price dynamics of 85% EPA over the past 6 months (Resource - Echemi.com) 5.5. Enlarged feasibility study Table 4 Name of indicator Meaning Lifetime of the Project, years 20 Production of stripped EPA (concentration 85%), tons per year 150 000 Operating costs, EUR/year 50 052 740 Cost of reduced EPA (concentration 85%), EUR/ton 376 Sale price of reduced EPA (concentration 85%), EUR/ton 700 The amount of electricity to be sold, kWh per year 56 866 617 Electricity sales price, EUR/kW*h 0,05 Annual income, EUR 93 242 088 Annual profit before tax, EUR 43 189 348 Tax burden (20%) 8 637 870 Net profit, EUR/year 34 551 478 Capital expenditures (including 10% contingencies), EUR 64 460 000 Discount rate 8% Payback period of investments without discounting, years 2,5 Payback period with discount, years 6,5 NPV pre-tax, EUR 278 766 411 NPV after-tax, EUR 211 215 382 IRR pre-tax 47% IRR after-tax 39% 16 5.6. Total number of personnel Table 5 Object Quantity Sulfuric acid shop and power unit 180 EFC workshop 75 Administration, technical and support services 70 TOTAL 325 17 6. List of materials used 1. Production of ammonia, mineral fertilizers and inorganic acids / Information and technical guide on the best available technologies ITS 2-2015 // NTD Bureau, Moscow 2015. 2.. Integrated Pollution Prevention and Control, Reference Document on Best Available Techniques for the Manufacture of Large Volume Inorganic Chemicals - Ammonia, Acids and Fertilisers, EUROPEAN COMMISSION August 2007 3. Results of a comprehensive assessment of overburden rocks of the Toolsa phosphorite deposit / Kizimägi E., Teodumäe A.// Izv. AN Estonian SSR. -1979. - No. 3. - pp. 243-250 4. Mineral composition of shell (obol) phosphorites of Estonia / H.N. Heinsalu, L.I. 5. Guidelines for the application of the Classification of reserves of deposits and predicted resources of solid minerals, Phosphate ores, Moscow, 2007 6. Abstracts of the All-Union Seminar “Material Composition of Phosphorites”, May 11-13, 1977, Novosibirsk 7. Comparative characteristics of Syrian phosphorite - raw materials of phosphorus-containing mineral fertilizers, Klimenko R.N., UDC 661.152, Bulletin of KDU im..M. Ostrogradsky, Issue 5/2010 (64) part 1 8. Estonian Planning Law 9. Estonian Industrial Emissions Act 10. Estonian Law on Environmental Impact Assessment and Environmental Management System 11. Agricultural Market Information System 12. DAP fertilizer - Monthly Price - Commodity Prices - Price Charts, Data, and News - IndexMundi 13. Rock Phosphate - Monthly Price - Commodity Prices - Price Charts, Data, and News - IndexMundi 14. Yara report 2 quarter 2018 15. Market of mineral fertilizers, National Research University, Higher School of Economics, 2017 18 Saatja: <[email protected]> Saadetud: 07.06.2023 12:41 Adressaat: <"MKM info"> Teema: Fwd: Re: reg. Fertilizers project in Estonia Manused: Baltic Phosphate_FS_Fertilizers_in_Aseri_port.pdf Dear Sirs! I have sent the letter to contacts I have from 2021, but to be sure also send copy to general e-mail in case you have changes in management. So: We would like to raise our project of Phosphorites exploration and further production of NP, NPK fertilizers in Aseri industrial zone (also port Aseri project). Wed like to know what is the current status of decision on phosphorites mining in Estonia. Our company ready to launch mining itself or buy ore. Could you please inform when licenses for mining will be places for sale? I attach here our projects to remind what are our goals. Can we arrange a meeting in a period of 20-27 June in Tallinn to discuss prospectives of phosphoric topic? Dmytro Nikulin, our Member of the Board will tell more details. regards, Alex Sadovsky Chemtrade Estonia OU / Baltic Phosphate OU +372-5699-5117 21/01/2019 08:55, Kaupo Reede написав: > Hi, > > [email protected] > > Kaupo > > -----Original Message----- > From: [email protected] [mailto:[email protected]] > Sent: Friday, January 18, 2019 5:40 PM > To: Kaupo Reede <[email protected]> > Subject: Re: reg. Fertilizers project (in addition to the visit of > Dmytro Nikulin) > > Dear Mr. Reede, > > No, I have not. > Seems due to holidays we miss to contact each other. > Could you please remind theirs contacts? > > Alex > > 18/01/2019 16:31, Kaupo Reede написав: >> Dear Alex, >> >> Does you have contact with Allan Selirand or his colleagues? >> >> Lugupidamisega, >> >> Kaupo Reede >> >> Sent from my iPhone >> >>> On 18 Jan 2019, at 14:57, "[email protected]" >>> <[email protected]> wrote: >>> >>> Dear Mr. Reede, >>> >>> Will it be convenient for you to meet Dmytro Nukulin reg. >>> Phosphorites-fertilizers project on 24th Jan in Tallinn? >>> >>> regards, >>> Alex >>> >>> 06/12/2018 09:10, Kaupo Reede написав: >>>> Dear Mr Sadovsky, >>>> At first I would thank you for interest to invest to Estonia. >>>> Ofcourse we can help you in diferent procedures. For this we have >>>> special team and they obligation is to help foreigen investors in >>>> investmen processes. >>>> Allan, please kontakt with Mr Sadovsky. >>>> With best regards, >>>> Kaupo Reede >>>> Director of Economic Develompment Department Ministry of Economic >>>> Affairs and Communication -----Original Message----- >>>> From: Ene Jürjens >>>> Sent: Wednesday, December 05, 2018 2:38 PM >>>> To: [email protected] >>>> Cc: Kaupo Reede <[email protected]> >>>> Subject: RE: reg. Fertilizers project (in addition to the visit of >>>> Dmytro Nikulin) Dear Mr Sadovsky, Thank you for your e-mail and >>>> additional information. Very interesting project, indeed. >>>> I introduced your idea to Mr Kaupo Reede, who is Head of the >>>> Department of Economic Development. Hopefully they will respond you >>>> soon and provide you the information you asked for. >>>> Kind regards >>>> Ene Jürjens >>>> Ene Jürjens, PhD >>>> Maapõueressursside valdkonna juht | Majandus-ja >>>> Kommunikatsiooniministeerium Head of Mineral Resources Division | >>>> Ministry of Economic Affairs and Communication tel (+372) 625 6327 | >>>> mob (+372) 518 4031 [email protected] www.mkm.ee -----Original >>>> Message----- >>>> From: [email protected] <[email protected]> >>>> Sent: Monday, December 3, 2018 6:55 PM >>>> To: Ene Jürjens <[email protected]> >>>> Subject: reg. Fertilizers project (in addition to the visit of >>>> Dmytro >>>> Nikulin) >>>> Dear Dr. Ene Kadastik, >>>> Further to the visit of Dmytro Nikulin, Head of Chemtrade Estonia >>>> OU, regarding the project of Phosphoric fertilizers factory in >>>> Estonia we send you now a general view of the project. >>>> Kindly take look and send us a feedback with your opinion on how to >>>> make it suitable for Estonian economy and enviroment. >>>> What can you suggest in a matter of construction site disposition, >>>> infrastructure: gas, railway and electricity connection? >>>> With your help we hope to move on to the next stage of the project >>>> in the shorest time. >>>> regards, >>>> Alex Sadovsky >>>> Commercial Director >>>> Chemrade Estonia OU >>>> +372-569-95-117 (Viber, WhatsApp, WeChat) >>>> [email protected]