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Carbon materials · Recarburizers

Calcined petroleum coke recarburizer

Aliases: CPC recarburizer · Calcined-petcoke carbon raiser

This page explains the product's principal composition, application directions and inquiry points; confirm the grade, guaranteed indicators, sizing, packing and process fit before quotation.

Steel / iron recarburizingCharge-carbon balanceValidated cost/residual selection
View grades and specifications
Calcined petroleum coke recarburizer · Product form reference
Product codeCH-RECARB-CPC
Industry application3
Key indicatorsGreen-coke source / coke type / calciner · Fixed C / ash / volatile matter / moisture · S / N / H / P / metals · Bulk / real density / calcination state / dissolution
Order boundaryQuotation and order confirmation

QUICK DECISION

Four answers before reading the technical detail

This section supports initial screening; final grade, addition and effects require operating conditions, formal documents and plant validation.

01

What it is

This page explains the product's principal composition, application directions and inquiry points; confirm the grade, guaranteed indicators, sizing, packing and process fit before quotation.

02

What it does

  • Steel / iron recarburizing
  • Charge-carbon balance
  • Validated cost/residual selection
03

Where it fits

  • Charging and melting; late steel trimming requires dedicated validation
  • Charging, mid-melt or pre-tap adjustment with sufficient dissolution time
  • Charging and melting, with controlled trimming where needed
04

Boundary not to miss

  • Sulfur, nitrogen, volatiles, ash, green-coke variability and incomplete late dissolution can create chemistry, inclusion, gas or recovery risks
  • Anode-grade CPC identity, typical properties or another supplier's data must not be transcribed as this product's guarantees
  • Do not default to ductile iron or CGI without reviewing S/N/H and source variation

SELECTION BOUNDARY

Start with the selection boundary

CPC is calcined petroleum coke—not green petroleum coke, ordinary fuel petcoke, graphitized petcoke or EAF injection carbon. Selection must compare source, calcination state, S/N/H, ash, volatiles, sizing and furnace-specific absorption; fixed carbon alone cannot justify substitution for graphitized or anthracite routes.

PRODUCT MANUFACTURING

Manufacturing process and identity boundary

Calcined-petcoke recarburizer is produced by controlled calcining of verified green petroleum coke in a rotary kiln, pot calciner, shaft kiln or another supplier-declared unit to reduce moisture/volatiles and alter density/reactivity, followed by cooling, crushing, screening, homogenisation, sampling and lot testing. Equipment, thermal schedule, coke type and any blending must be disclosed by the actual supplier; the page does not imply that Jinsheng owns a calciner.

  1. 01Verify green-petcoke source, coke type, S/N/metal residuals and lot traceability
  2. 02Calcine under control in the declared rotary, pot, shaft or other unit
  3. 03Cool under control and prevent moisture pickup, oxidation, oil and foreign matter
  4. 04Crush, screen, control fines and homogenise for the actual product
  5. 05Sample and test calcination state, chemistry, sizing and properties before packing

SPECIFICATIONS & PACKAGING

Grades, RFQ parameters, indicators and documents

Beyond fixed carbon, a CPC RFQ must confirm green-coke source/type, calciner and calcination state, ash, volatiles, moisture, S/N/H/P and metallic residuals, sizing/fines/oversize, bulk or real density where relevant, dissolution and plant absorption validation. Typical anode-grade CPC data do not automatically become a metallurgical-recarburizer specification.

  1. 01Fix CPC application identity, green-coke source/type, calciner and supplier traceability
  2. 02Agree fixed carbon, ash, volatiles, moisture and S/N/H/P/metal residuals
  3. 03Agree full sizing, fines, oversize and bulk/real-density methods
  4. 04When calcination state, dissolution or absorption is accepted, first define the test/furnace-trial basis
  5. 05Reconcile TDS, SDS/PSI, contract, lot COA and label without borrowing anode data

GRADES & SPECIFICATIONS

Grades, specifications, indicators and packaging

Supply specifications, packaging, lead time and quality documents are subject to the formal quotation and order confirmation.

Grade / familyChemistrySize and formPackaging
Specification direction 01Calcined petroleum coke recarburizerConfirm grade, applicable standard and guaranteed values before quotation
  • Green-coke source / coke type / calcinerConfirm in inquiry
  • Fixed C / ash / volatile matter / moistureConfirm in inquiry
  • S / N / H / P / metalsConfirm in inquiry
  • Bulk / real density / calcination state / dissolutionConfirm in inquiry

Confirm against the addition method, equipment and order requirements

Confirm pack format, net weight and labels in the quotation and order

ORDER SPECIFICATION CONFIRMATION

What must be confirmed before this becomes an order specification

Supply specifications, packaging, lead time and quality documents are subject to the formal quotation and order confirmation.

  1. 01Confirm the product, grade, application and supply scope
  2. 02Fix guaranteed chemistry, sizing, form and packing in the quotation and order
  3. 03Agree sampling, test methods, acceptance rules and lot COA fields
  4. 04Confirm the required TDS, SDS/PSI, labels and delivery documents

SELECTION AND COMPARISON

Compare specification directions by indicators and operating conditions

Supply specifications, packaging, lead time and quality documents are subject to the formal quotation and order confirmation.

01Specification direction

Calcined petroleum coke recarburizer

Compare the key indicators below, then confirm grade, guaranteed values, sizing and packing against the operating conditions.

Key indicators
Green-coke source / coke type / calcinerFixed C / ash / volatile matter / moistureS / N / H / P / metalsBulk / real density / calcination state / dissolution
Size and form
Confirm against the addition method, equipment and order requirements
Packaging
Confirm in the quotation and order

INDUSTRY APPLICATION

Industry, furnace, material and addition point

Confirm the process position before method and quantity calculations; an application relationship for one furnace or material must not be copied to another.

01

Steelmaking plants

Charging and melting; late steel trimming requires dedicated validation

Furnace / equipment
EAF and validated induction-melting routes
Material / output
Steel grades whose sulfur, nitrogen, volatile, ash and metallic-residual budgets permit CPC
02

Steel foundries

Charging, mid-melt or pre-tap adjustment with sufficient dissolution time

Furnace / equipment
EAF or coreless induction furnace
Material / output
Process-validated carbon and alloy cast steels with a residual budget
03

Iron foundries

Charging and melting, with controlled trimming where needed

Furnace / equipment
Coreless induction furnaces and validated duplex routes
Material / output
Grey iron; ductile iron and CGI only after approval of S/N/H and nodularisation-interference risks

APPLICATION METHOD

Application, calculation, effect and risk validation

CPC may be used for charging or melting-stage recarburizing in reviewed EAF steel, cast steel and induction-melted cast iron; ductile iron/CGI first requires review of S/N/H and nodularisation interference. It is not a one-for-one substitute for graphitized petcoke on fixed carbon alone and is not EAF injection carbon.Use decimal mass fractions for the starting estimate: ⟦m_add(kg) ≈ M_melt(t) × 1,000 × Δw_C ÷ (w_C,product × η_C)⟧. Δw_C must deduct charge-carbon carry-in and predicted oxidation/decarburisation; w_C,product comes from the actual lot; η_C must come from a site trial on the same furnace, sizing and addition point. The equation does not replace heat-by-heat resampling or create a fixed kg/t commitment.

  1. 01Confirm metal grade, furnace, charge carbon, oxidation loss and S/N/H/ash budgets
  2. 02Calculate the start amount from actual-lot fixed carbon and furnace CPC absorption history
  3. 03Add in stages at a charging/melting point favourable to contact, wetting and stirring
  4. 04Observe flotation and slag, allow dissolution time and resample C and constrained elements
  5. 05Correct CPC η_C independently from heat results; do not borrow GPC or anthracite data

PROBLEM AND SOLUTION

From operating objective to effect verification

Each application explains the role, method, quantity principle and risk boundary; the final proposal is confirmed against operating conditions and lot documents.

01

Steelmaking plants

Charging and melting; late steel trimming requires dedicated validation

Furnace / equipment
EAF and validated induction-melting routes
Material / output
Steel grades whose sulfur, nitrogen, volatile, ash and metallic-residual budgets permit CPC
Method
Add in stages from charge carbon, oxidation loss, slag, sizing, wetting and stirring, leaving sufficient time for dissolution and resampling.
Quantity determination
Use decimal mass fractions consistently. General estimate: ⟦m_add(kg) ≈ M_melt(t) × 1,000 × Δw_C ÷ (w_C,product × η_C)⟧. Δw_C is the net carbon increase still required after charge-carbon carry-in and predicted oxidation/decarburisation; enter product carbon fraction w_C,product and the measured furnace-, size- and stage-specific carbon absorption η_C as decimals. The equation is only a starting estimate; heat-by-heat sampling and plant trials must correct the amount.
Expected effects
  • Closes the target carbon deficit within the residual and absorption window
Limits and risks
  • Sulfur, nitrogen, volatiles, ash, green-coke variability and incomplete late dissolution can create chemistry, inclusion, gas or recovery risks
02

Steel foundries

Charging, mid-melt or pre-tap adjustment with sufficient dissolution time

Furnace / equipment
EAF or coreless induction furnace
Material / output
Process-validated carbon and alloy cast steels with a residual budget
Method
Calculate from measured chemistry and furnace-specific absorption, use a practice that promotes contact, wetting and stirring, and resample before tapping.
Quantity determination
Use decimal mass fractions consistently. General estimate: ⟦m_add(kg) ≈ M_melt(t) × 1,000 × Δw_C ÷ (w_C,product × η_C)⟧. Δw_C is the net carbon increase still required after charge-carbon carry-in and predicted oxidation/decarburisation; enter product carbon fraction w_C,product and the measured furnace-, size- and stage-specific carbon absorption η_C as decimals. The equation is only a starting estimate; heat-by-heat sampling and plant trials must correct the amount.
Expected effects
  • Corrects the cast-steel charge-carbon balance
Limits and risks
  • Anode-grade CPC identity, typical properties or another supplier's data must not be transcribed as this product's guarantees
03

Iron foundries

Charging and melting, with controlled trimming where needed

Furnace / equipment
Coreless induction furnaces and validated duplex routes
Material / output
Grey iron; ductile iron and CGI only after approval of S/N/H and nodularisation-interference risks
Method
Charge with metallic feed to promote contact and absorption; ductile/CGI practice must also review base-iron sulfur, nitrogen, pinhole and downstream Mg-treatment windows.
Quantity determination
Use decimal mass fractions consistently. General estimate: ⟦m_add(kg) ≈ M_melt(t) × 1,000 × Δw_C ÷ (w_C,product × η_C)⟧. Δw_C is the net carbon increase still required after charge-carbon carry-in and predicted oxidation/decarburisation; enter product carbon fraction w_C,product and the measured furnace-, size- and stage-specific carbon absorption η_C as decimals. The equation is only a starting estimate; heat-by-heat sampling and plant trials must correct the amount.
Expected effects
  • Adds carbon in an approved grey-iron or base-iron practice
Limits and risks
  • Do not default to ductile iron or CGI without reviewing S/N/H and source variation

STORAGE & SAFETY

Storage, handling and risk

  • Keep dry and isolated from oil and foreign matter; manage fines as combustible dust and prevent dispersion.
  • Wet petcoke or material of unknown identity/calcination state must not be introduced directly into molten metal.

This section does not replace the company's final SDS/PSI or the plant safety procedure.

REFERENCE AND ORDER BOUNDARY

Use industry references to understand, then order documents to confirm

Supply specifications, packaging, lead time and quality documents are subject to the formal quotation and order confirmation.

DOCUMENTS & MEDIA

Images, TDS, SDS and COA

Document availability depends on the product, lot, destination market and order agreement.

TDS

Confirms product identity, guaranteed indicators, sizing, form and packing.

SDS / PSI

Confirms storage, handling, protection and market-specific safety information.

COA

Links a specific lot to test items, results, methods and issue information.

INDUSTRY TECHNICAL REFERENCES

Selected external reference material

The following items come from licensed public media or original producer websites and explain similar products or typical processes only. They are not Jinsheng photographs, TDS, SDS or lot COA and create no supply commitment.

Blank COA template

COA field template (not a certificate)

A blank structure for lot, chemistry, sizing, method, disposition and issue data. It contains no test result and cannot be used for delivery.

Jinsheng blank COA field template · 2026-08-14Open field template

SOURCES

Public references and verification dates

  1. YB/T 192—2015 Carbon raiser for steelmaking, official recordStandard · 2026-08-21
  2. JB/T 14236—2023 Recarburizer for foundry, official recordStandard · 2026-08-21
  3. Rain Carbon: official technical paper on calcining petroleum coke into CPCManufacturer source · 2026-08-21
  4. Elkem Carbon Slovakia: gas-calcined-anthracite recarburizers and CPC blendsManufacturer source · 2026-08-21
  5. Elkem: recarburizer use, dissolution and casting-defect risksManufacturer source · 2026-08-21

Public sources supplement general facts; they do not replace Jinsheng's formal product specification, TDS or lot COA.

INQUIRY PREPARATION

Prepare these operating conditions for a more precise technical response

Please provide the specification, quantity, destination, and contact information.

Already includedCH-RECARB-CPCCalcined petroleum coke recarburizer
  1. 01Target industry, steel grade or casting material
  2. 02Furnace type, equipment, melt weight and current operating practice
  3. 03Measured chemistry, target chemistry and permitted residuals
  4. 04Planned addition point, temperature, slag and stirring conditions
  5. 05Current product, addition, recovery or operating-issue record
  6. 06Required size, form, packaging, quantity and destination
  7. 07Available melt analysis, microscopy, photographs or trial results

TECHNICAL AND QUOTATION CONSULTATION

Send the operating conditions for human review

Domestic inquiries are handled by the Domestic Sales Department and international inquiries by the International Sales Department. Price, availability and lead time are confirmed for each inquiry based on specification, quantity and delivery location.