Glass-Lined Reactor, F Type

Glass-Lined Reactor, F Type
  • Glass-Lined Reactor, F Type
  • Glass-Lined Reactor, F Type
  • Glass-Lined Reactor, F Type
  • Glass-Lined Reactor, F Type
    • F Type

    Glass-Lined Reactor

    Features

    • The F type glass lined reactor comes with a one-piece design that the cover and body can not be separated. Due to that, a manhole has to be designed on the head of the reactor to make it easy for operators to enter the reactor to carry out maintenance and parts replacement.
    • It is a large capacity industrial process reactor, suitable for large scale production environment.
    • Similar to the K-type reactor, this type of chemical reactor is manufactured using TJ09/TJ16/TJ21S high end enamel and skilled enameling process. This enables the glass lining to be remarkably corrosion resistant, impact resistant and temperature variation resistant, combined with less prone to fracture and high durability.
    • Taiji is able to design and manufacture non standard glass lined reactor to user's requirements.
    • Our F type glass lined steel reactor comes in complete specifications, including F1500L, F2000L, F3000L, F4000L, F5000L, F6300L, F8000L, F10000L, F12500L, F16000L, F20000L, F30000L, F40000L, F45000L, F50000L, F60000L, F70000L, F90000L, etc.
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    • Glass-Lined Reactor, K Type
    • Glass-Lined Reactor, K Type
    • Glass-Lined Reactor, K Type
    • Glass-Lined Reactor, K Type
    • Glass-Lined Reactor, K Type
    • Glass-Lined Reactor, K Type
    • Glass-Lined Reactor, K Type
    • Glass-Lined Reactor, K Type
    Technical Parameters of the Glass-Lined Reactor
    Technical Parameters of the Glass-Lined Reactor

    • F1500L- F6300L Glass-Lined Reactor
    • F1500L- F6300L Glass-Lined Reactor
    • F1500L- F6300L Glass-Lined Reactor
      F1500L- F6300L Design Drawing (Plan View)
      Internal Vessel Jacket
    Design Pressure
    (MPa)    		 0.4 0.6
    Design Temperature
    ( ℃ )    		 -19 ~200 -19 ~200
    Model F 1500 F 2000 F 3000 F 4000 F 5000 F 6300
    Nominal Capacity (L) 1500 2000 3000 4000 5000 6300
    Total Capacity (L) 2020 2470 3860 4795 6040 6900
    Calculated Capacity (Note 1) (L) 1990 2440 3830 4765 6016 6872
    Jacket Capacity (L) 301 390 495 805 898 1015
    Heat Exchange Area (m²) 5.92 7.31 9.98 12.44 14.06 16.36
    Half-Pipe Coil Heat Exchange Area (m²) 2.5 3.5 4.3 6.0 7.2 8.5
    Reference Weight (kg) 1975 2230 3300 3750 4570 5050
    Dimensions (mm) d1 1300 1300 1600 1600 1750 1750
    d2 1450 1450 1750 1750 1900 1900
    d3 (Note 2) 1915 1915 2221 2221 2412 2412
    d4 680 680 720 720 720 720
    d5 700 700 800 800 850 850
    h1 1801 2136 2250 2730 2888 3244
    h2 190 190 190 190 190 190
    h3 725 725 700 700 750 750
    h4 975 975 1060 1060 1200 1200
    B1 315 315 315 315 350 350
    B2 400 400 450 450 500 500
    Φ 30 30 30 30 30 30
    Vessel Nozzle DN (mm) a 300x400 300x400 300x400 300x400 300x400 300x400
    b 125 125 150 150 150 150
    C 100 100 100 100 125 125
    d 100 100 100 100 125 125
    e 125 125 125 125 125 125
    f 125 125 125 125 150 150
    g 100 100 100 100 125 125
    h 125 125 125 125 150 150
      100 100 125 125 125 125
    Jacket Nozzle DN (Note 3) (mm) k1 40/50 40/50 65/50 65/50 65/50 65/50
    k2 40 40 65 65 65 65
    k3 40/50 40/50 65/50 65/50 65/50 65/50
    k4 40 40 65 65 65 65
    m G3/8” G3/8” G3/8” G3/8” G3/8” G3/8”
    Drive (Note 4) (mm) dN 80 80 95 95 95 95
    h5 1580 1580 1680 1680 1680 1780

    Notes

    • Calculated Capacity
      Volume: Measures the capacity below the high neck flange. This does not include the volume taken up by the flange itself.
    • Support Options
      The type of support used to hold the reactor can be specified by the customer when placing an order. If no preference is indicated, the default support type will be lugs attached to the exterior.
    • k1 and k3 Values
      The dimensions k1 and k3 will vary depending on whether the reactor has a full jacket or half pipe heating/cooling system.
      For a full jacket, use the values listed before the slash (/)
      For half pipes, use the values after the slash (/)
    • Drive Device Parameters
      Reference Only: The provided drive device parameters are for reference purposes.
      Actual Selection: The final selection of the rack reducer type will be determined based on the specific requirements of the application.

    • F8000-F20000L Glass-Lined Reactor
    • F8000-F20000L Glass-Lined Reactor
    • F8000-F20000L Glass-Lined Reactor
      F8000L Design Drawing (Plan View)
    • F8000-F20000L Glass-Lined Reactor
      F10000L-20000L Design Drawing (Plan View)
      Internal Vessel Jacket
    Design Pressure
    (MPa)    		 0.4 0.6
    Design Temperature
    ( ℃ )    		 -19~200 -19~200
    Model F 8000 F 10000 F 12500 F 16000 F 20000
    Nominal Capacity (L) 8000 10000 12500 16000 20000
    Total Capacity (L) 9138 11757 13733 17491 21835
    Calculated Capacity (Note 1) (L) 9110 11724 13700 17446 21790
    Jacket Capacity (L) 1666 1940 2243 2551 2870
    Heat Exchange Area (m²) 18.38 21.35 24.89 29.48 34.04
    Half-Pipe Coil Heat Exchange Area (m²) 8.9 10.3 12.4 14.5 16.5
    Reference Weight (kg) 6780 7670 9120 11300 13700
    Dimensions (mm) d0 800 800 800 800 900
    d1 2000 2200 2200 2400 2600
    d2 2200 2400 2400 2600 2800
    d3 (Note 2) 2763 2964 2964 3238 3439
    d4 880 980 980 980 1080
    d5 1100 1200 1200 1200 1300
    h1 3310 3533 4053 4346 4641
    h2 210 210 210 210 210
    h3 850 900 900 950 1000
    h4 1250 1300 1300 1500 1550
    h 5680 5890 6440 6770 7350
    B1 400 470 470 470 470
    B2 700 700 700 700 700
    Φ 36 36 36 36 36
    Vessel Nozzle DN (mm) a 125 150 150 150 150
    C 300x400 300x400 300x400 450 450
    d 200 200 200 200 250
    e1 200 200 200 200 200
    e2 150 200 200 200 200
    g1 150 150 150 150 150
    g2 150 150 150 150 150
    g3 150 150 150 150 150
    g4 / 150 150 150 150
    S 125 125 125 125 125
    k 125 125 125 125 125
    Jacket Nozzle DN (Note 3) (mm) b1 65/65 80/65 80/65 100/65 100/65
    b2 65 80 80 100 100
    b3 65/65 80/65 80/65 100/65 100/65
    b4 65 80 80 100 100
    m G3/4° G3/4” G3/4 G3/4” G3/4*
    n G1/2" G1/2” G1/2” G1/2” G1/2”
    Drive (Note 4) (mm) dN 110 110 110 130 140
    h5 1960 1960 1990 2020 2300

    Notes

    • Calculated Capacity
      Volume: Measures the capacity below the high neck flange. This does not include the volume taken up by the flange itself.
    • Support Options
      The type of support used to hold the reactor can be specified by the customer when placing an order. If no preference is indicated, the default support type will be lugs attached to the exterior.
    • b1 and b3 Values
      The dimensions b1 and b3 will vary depending on whether the reactor has a full jacket or half pipe heating/cooling system.
      For a full jacket, use the values listed before the slash (/)
      For half pipes, use the values after the slash (/)
    • Drive Device Parameters
      Reference Only: The provided drive device parameters are for reference purposes.
      Actual Selection: The final selection of the rack reducer type will be determined based on the specific requirements of the application.

    • F30000-F90000 Glass-Lined Reactor
    • F30000-F90000 Glass-Lined Reactor
      F30000L-50000L Design Drawing (Plan View)
    • F30000-F90000 Glass-Lined Reactor
      F60000L-90000L Design Drawing (Plan View)
    Model F 30000 F 40000 F 45000 F 50000 F 60000 F 70000 F 90000
    Nominal Capacity (L) 30000 40000 45000 50000 60000 70000 90000
    Total Capacity (L) 33645 44900 51380 56470 64652 75290 93110
    Calculated Capacity (Note 1) (L) 33500 44000 52180 55510 63641 74300 92110
    Jacket Capacity (L) 3700 3800 4350 4520 5080 7350 9110
    Heat Exchange Area (m²) 45.0 48.4 50.2 60 68.5 76.5 95.2
    Reference Weight (kg) 20000 26520 29650 32155 36380 47950 61000
    Dimensions (mm) d0 1100 1600 1600 1750 1750 1750 1750
    d1 3000 3600 3600 3800 3800 4000 4000
    d2 3200 3800 3800 4000 4000 4200 4200
    d4 1300 1400 1400 1600 1600 1600 1600
    d5 1300 1400 1400 1600 1600 1600 1600
    d6 (Note 2) 2300 2520 2520 2680 / / /
    h1 5340 5000 5731 5611 6311 6692 8071
    h2 260 609 609 647 667 667 667
    h3 1150 1300 1300 1340 1340 1600 1600
    h 8985 9040 9770 9790 10500 13000 14450
    B 470 470 470 470 470 700 700
    φ 24 30 30 30 / / /
    Vessel Nozzle DN (mm) a 150 150 150 150 150 150 150
    C 450 450 450 450 450 450 450
    d 250 250 250 250 250 300 300
    e1 200 200 200 200 200 200 200
    e2 200 200 200 200 200 200 200
    e3 / 200 200 200 200 200 200
    g1 150 150 150 150 150 150 150
    g2 150 150 150 150 150 150 150
    g3 150 150 150 150 150 150 150
    g4 150 150 150 150 150 150 150
    S 125 125 125 125 125 125 125
    k 125 125 125 250 250 250 250
    Jacket Nozzle DN (mm) b1 100 125 125 125 125 125 125
    b2 100 125 125 125 125 125 125
    b3 100 125 125 125 125 125 125
    b4 100 125 125 125 125 125 125
    m G3/4” G3/4” G3/4” G3/4” G3/4” G3/4” G3/4”
    n G1/2” G1/2” G1/2” G1/2” G1/2” G1/2” G1/2”
    Drive (Note 3) (mm) dN 160 160 160 180 200 240 273
    h5 2570 2610 2610 2710 3420 3970 4170

    Notes

    • Calculated Capacity
      Volume: Measures the capacity below the high neck flange. This does not include the volume taken up by the flange itself.
    • Support Type
      Customizable by the user. In the absence of a specific request, B-type support legs will be used. For specifications above F60000L, a skirt support is recommended.
    • Drive Device Parameters
      These parameters are for reference only. The actual rack reducer type will be selected based on specific requirements.

    • Q630L-Q16000L Glass-Lined Reactor
    • Q630L-Q16000L Glass-Lined Reactor
      Q630L-Q6300L Design Drawing (Plan View)
    • Q630L-Q16000L Glass-Lined Reactor
      Q8000L Design Drawing (Plan View)
    • Q630L-Q16000L Glass-Lined Reactor
      Q10000L-Q16000L Design Drawing (Plan View)
      Internal Vessel Jacket
    Design Pressure
    (MPa)    		 -0.1/0.6/1.0 0.6
    Design Temperature
    ( ℃ )    		 -19~200 -19~200
    Model Q630 Q1000 Q1500 Q2000 Q3000 Q4000 Q5000 Q6300 Q8000 Q10000 Q12500
    Nominal Capacity (L) 630 1000 1500 2000 3000 4000 5000 6300 8000 10000 12500 16000
    Total Capacity (L) 890 1470 2130 2575 3811 4780 6040 6900 9105 11719 13696 17491
    Jacket Capacity (L) 147 206 301 390 495 805 898 1015 1666 1940 2243 2551
    Heat Exchange Area (m²) 3.35 4.55 5.92 7.31 9.98 12.44 14.06 16.36 18.38 21.35 24.89 29.48
    Reference Weight (kg) 1055 1865 1963 2175 3205 3522 4580 5060 6718 7670 9101 10954
    Dimensions (mm) d1 1000 1200 1300 1300 1600 1600 1750 1750 2000 2200 2200 2400
    d2 1100 1300 1450 1450 1750 1750 1900 1900 2200 2400 2400 2600
    d3 (Note 1) 1276 1477 1655 1655 1956 1956 2152 2152 2452 2703 2703 2908
    h1 1385 1560 1766 2131 2250 2730 2888 3244 3320 3543 4063 4356
    h3 595 650 699 699 700 700 750 750 860 910 910 960
    h4 815 910 940 940 1060 1060 1200 1200 1210 1310 1310 1410
    B1 400 400 400 400 400 400 400 400 400 470 470 470
    B2 / / 510 510 510 510 510 510 510 550 550 550
    Φ 30 30 30 30 30 30 30 30 30 36 36 36
    Vessel Nozzle DN (mm) M 125 125 125 125 150 150 150 150 200 200 200 200
    L 100 100 100 100 125 125 125 125 125 150 150 150
    N1 300X400 300X400 300X400 300X400 350X450 350X450 350X450 350X450 500 500 500 600
    N2 100 125 125 125 150 150 200 200 200 200 200 200
    N3 100 100 100 100 100 100 125 125 150 150 150 150
    N4 100 100 125 125 125 125 125 125 150 150 150 150
    N5 100 125 125 125 125 125 150 150 125 125 125 125
    N6 100 100 100 100 100 100 125 125 150 150 150 150
    N7 100 100 125 125 125 125 125 125 150 200 200 200
    N8 / / / / / / / / 125 125 125 125
    N9 / / / / / / / / / 150 150 150
    Jacket Nozzle DN (mm) N11 32 32 40 40 50 50 65 65 65 80 80 100
    N12 32 32 40 40 50 50 65 65 65 80 80 100
    N13 32 32 40 40 50 50 65 65 65 80 80 100
    N14 / / /     / 65 65 65 80 80 100
    N15 / / 50 50 65 65 65 65 65 80 80 100
    N16 / / 50 50 65 65 65 65 65 80 80 100
    N17 G3/8” G3/8” G3/8” G3/8” G3/8” G3/8” G3/8” G3/8” G3/4” G3/4” G3/4” G3/4”
    N18 G1/2” G1/2” G1/2” G1/2” G1/2” G1/2” G1/2” G1/2” G1/2” G1/2” G1/2” G1/2”
    Drive (mm) dN 65 80 80 80 95 95 95 95 110 110 110 130
    h 680 720 720 720 785 785 785 785 840 840 840 820
    Notes
    Support Options: The type of support used to hold the reactor can be specified by the customer when placing an order. If no preference is indicated, the default support type will be lugs attached to the exterior.
    What are the differences between K type and F type glass-lined reactors?

    Unlike the K-type glass-lined reactor, the F-type glass-lined reactor is designed with integrated vessel head and vessel body. A manway is provided on top for internal inspection and component replacement.

    The K-type glass-lined reactors, instead, are designed with removable head structure. The vessel head is connected to the vessel body with gasket and clamps for easy disassembly and maintenance, and more accessible agitation system.

    The K-type glass-lined reactors are available in capacities from 50 to 16,000 L, which are more suitable for small- and medium-capacity production; the F-type glass-lined reactors are designed for medium- and large-scale industrial production and are available in capacities from 1,500 to 90,000 L. Therefore, the F-type glass-lined reactors are more suitable for high-volume production in chemical, pharmaceutical, and agrochemical industries.

    Both types of glass-lined reactors can be configured with agitation system, heat transfer system and related components. Specific models should be selected according to production capacity, maintenance requirements, agitation requirements and process conditions.

    Applications

    The glass-lined reactor (F-type) is primarily used for medium- and large-scale industrial reaction processes during the production of pharmaceuticals, pesticides and agrochemicals, fine chemicals, basic chemicals, dyes and pigments, and other chemical products.

    Depending on the specific materials and process conditions, the glass-lined reactor can be used for chemical synthesis, esterification, condensation, hydrolysis, polymerization, neutralization, chlorination, and other reaction, mixing, and temperature-control processes involving corrosive materials.

    Whether the glass-lined equipment can be used for a specific process should be determined according to material composition, concentration, temperature, pressure and actual reaction conditions.

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